阅读说明：本技术 多厕位移动智能净排wc系统总成及其污物处理方法 (Multi-toilet-station mobile intelligent clean-discharge WC system assembly and sewage treatment method thereof ) 是由 陈以浙 余江 冯国强 杨伟锋 范高慧 何永强 施王军 孙冉 周永强 陈天泯 许志 于 2020-12-16 设计创作，主要内容包括：本发明提供多厕位移动智能净排WC系统总成,它包括厕位使用子系统、风源子系统、粪便收集子系统、固液分离子系统、微波焚化子系统、无极光催化处理尿液处理子系统、无极光催化处理废气处理子系统、热交换系统、中水循环回用冲厕子系统及智能控制子系统共十大子系统；同时还提供了基于其系统总成的污物处理方法；它攻克了人类粪便排泄环境、疾病传播、损害身体健康的固液污物粪便快速灭菌、焚化处理、污水处理回用的技术障碍；采用全物理化学技术,集粪便收集、微波焚化、光催化降解、紫外杀菌、中水冲厕技术和智能控制系统于一体,实现人类排泄物的快速无害化处理,达到无色、无味和无二次污染的达标排放要求,各污染物排放技术指标达到国家标准。(The invention provides a multi-toilet-seat mobile intelligent WC (flushing) system assembly, which comprises ten subsystems, namely a toilet seat using subsystem, a wind source subsystem, an excrement collecting subsystem, a solid-liquid separation subsystem, a microwave incineration subsystem, an electrodeless photocatalytic treatment urine treatment subsystem, an electrodeless photocatalytic treatment waste gas treatment subsystem, a heat exchange system, a reclaimed water recycling toilet flushing subsystem and an intelligent control subsystem; simultaneously, a sewage treatment method based on the system assembly is also provided; the technical obstacles of human excrement discharge environment, disease transmission, quick sterilization of solid-liquid sewage, excrement incineration treatment and sewage treatment and recycling are overcome; the full physical chemistry technology is adopted, the excrement collection, the microwave incineration, the photocatalytic degradation, the ultraviolet sterilization, the reclaimed water toilet flushing technology and the intelligent control system are integrated, the quick harmless treatment of human excrement is realized, the discharge standard requirements of no color, no odor and no secondary pollution are met, and the discharge technical indexes of various pollutants reach the national standard.)

1. The utility model provides a many toilets remove intelligence net row WC system assembly which characterized in that: the system comprises ten subsystems, namely a toilet seat using subsystem, a wind source subsystem, an excrement collecting subsystem, a solid-liquid separation subsystem, a microwave incineration subsystem, an electrodeless photocatalytic treatment urine treatment subsystem, an electrodeless photocatalytic treatment waste gas treatment subsystem, a heat exchange system, a reclaimed water recycling toilet flushing subsystem and an intelligent control subsystem;

the toilet seat using subsystem: comprises a multi-toilet-room man-machine interface, which receives human excrement and has a self-cleaning function;

the wind source subsystem: the system provides proper compressed air for the whole system and performs storage, pressure regulation, air path control and pressure air delivery of the compressed air;

the feces collection subsystem: collecting excrement received by a human-computer interface of a plurality of toilet positions through vacuum negative pressure, and sending the collected excrement to a solid-liquid separation subsystem through positive pressure;

the solid-liquid separation subsystem: carrying out solid and liquid two-phase separation treatment on human excrement; inputting the upper layer urine into a microwave photocatalytic reaction system; the lower heavy phase is atomized and enters a microwave incineration system after being cut and crushed;

the microwave incineration subsystem: after heavy phase at the lower layer of the solid-liquid separation subsystem is atomized, the heavy phase is adsorbed by SiC in the microwave incineration subsystem for incineration treatment;

the system comprises an electrodeless photocatalytic treatment urine treatment subsystem: the upper urine separated by the solid-liquid separation subsystem is atomized by a nozzle and then sprayed into a microwave photochemical reactor for degradation and sterilization treatment, and the treated exhaust gas enters a heat exchange subsystem to cool and liquefy the moisture in the exhaust gas and flush toilet water; the purified tail gas is exhausted after passing through a photochemical reactor;

the electrodeless photocatalytic treatment waste gas treatment subsystem: the gas which is not liquefied in the microwave electrodeless photoreactor and the tail gas of the microwave incineration system enters the electrodeless photochemical reactor to be subjected to deodorization and organic gas degradation treatment, so that the safe and odorless emission standard is achieved;

the heat exchange system is as follows: wind energy is utilized in a multi-row pipe mode to cool, liquefy and recover moisture in the outer exhaust gas of the electrodeless photochemical reactor, and the moisture is sent to a reclaimed water recycling toilet flushing subsystem;

the recycled water recycling toilet flushing subsystem comprises: storing the water condensed and liquefied by the heat exchanger into a reclaimed water storage tank for flushing a toilet for recycling;

the intelligent control subsystem: the system provides the functions of automatic liquid level detection, automatic emission detection, gas-water electric control, human-computer interaction interface and Internet of things access for the whole system.

2. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the toilet seat using subsystem comprises: a bedpan (1), a bedpan washing nozzle (2) which is supplied with water by a washing valve of an air-water control device (177) through a bedpan washing water pipe (178), a bedpan washing water supply pipe system (3), a feces dropping opening (5) and a bedpan full liquid level switch (4); the bedpan (1) receives human excrement, after the excrement is discharged, a flushing button (173) is operated, the excrement collecting subsystem opens the quick excrement valve (7) through a first excrement valve control air pipe (179) under the control of the intelligent electric control device (172) and the air-water control device (177), excrement is quickly sucked into the excrement collecting box (9) under the action of vacuum pressure in the excrement collecting box (9), and when the quick excrement valve (7) is opened, the bedpan flushing water supply pipe system (3) supplies water with certain pressure, so that the bedpan flushing nozzle (2) sprays water to flush the bedpan (1); when the bedpan (1) is full of excrement, the bedpan full liquid level switch (4) outputs a bedpan flushing command, and the execution process of the command is consistent with the bedpan flushing command sent by the flushing button (173).

3. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the fecal collection subsystem includes: the rapid drainage device comprises a rapid drainage valve (7), a dirt collecting box (9) and a dirt emptying valve (18), wherein the main body of the dirt collecting box (9) is cylindrical and can repeatedly bear certain negative pressure and positive pressure, a dirt inlet (12), a dirt outlet (13), an inspection port (16), a vacuum suction port (11) connected with a dirt collecting box vacuumizing pipe (180) controlled by an air-water control device (177), a positive pressure air supply port (14) connected with a dirt collecting box positive pressure inflation pipe (181) controlled by the air-water control device (177), a first full liquid level sensor (15), a first drainage pipe (6), a second drainage pipe (8) and a third drainage pipe (17) are arranged on a box body;

when the intelligent electric control device (172) detects that the toilet seat in the toilet seat using subsystem is not used by people, namely the flushing button (173) is not pressed down, the air-water control device (177) sends a vacuumizing instruction, the vacuum generator starts to work to pump the dirt collecting box (9) to a certain vacuum degree and keep the vacuum degree in a certain range all the time, the vacuum pressure switch in the air-water control device (177) is used for controlling the upper limit value and the lower limit value of the vacuum degree range, when the vacuum degree in the dirt collecting box (9) is reduced to be below-10 KPa, the ejector automatically starts to work to pump the dirt collecting box (9) to be vacuumized until the vacuum degree in the dirt collecting box (9) reaches-25 KPa, and the ejector automatically stops working; the sewage collecting box (9) which is kept at a certain range of vacuum pressure prepares for flushing the bedpan (1); when a first full liquid level sensor (15) of the sewage collecting box (9) detects that the excrement collected in the sewage collecting box (9) is full, an instruction for emptying the sewage collecting box (9) is sent to an intelligent electric control device (172), at the moment, a flushing instruction for temporarily shielding and storing a bed pan (1) is sent, a quick drain valve (7) is kept in a closed state, an emptying instruction is sent to the sewage collecting box (9), an electromagnetic valve for emptying the sewage collecting box in an air-water control device (177) acts, 0.3MPa of compressed air is provided for the sewage collecting box (9), and meanwhile, an excrement emptying valve (18) is opened through a second drainage valve control air pipe (182) controlled by the air-water control device (177) to force the sewage collecting box (9) to be emptied; the volume of the sewage collecting box (9) is unchanged, so the emptying time of the sewage collecting box is limited, after the set time is continued, the sewage collecting box emptying electromagnetic valve and the sewage emptying valve (18) in the air-water control device (177) are simultaneously closed, the vacuumizing procedure of the sewage collecting box (9) is automatically switched in, after the vacuum pressure in the sewage collecting box (9) meets the set requirement, the intelligent electric control device (172) firstly detects whether a flushing instruction of the temporarily shielded bedpan (1) exists, if so, the cleaning process of the bedpan (1) is immediately executed, if not, the flushing instruction of the bedpan (1) is switched in, and the sewage collecting box (9) is kept in a vacuum negative pressure state.

4. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the solid-liquid separation subsystem comprises: solid-liquid separation case (20), dirty entry (23) of excrement, heavy phase solid form export (24), deposit foul solution export (27), supernatant export (28), foul solution overflow outlet (29), foul solution returns entry (30), first foul smell discharge port (31), self-cleaning primary filter screen is constituteed (35), self-cleaning secondary filter screen is constituteed (32), swift current puts filter (25), primary filter screen washes compressed air supply inlet (34), secondary filter screen washes compressed air supply inlet (33), full liquid level switch (21), half liquid level switch (47), low liquid level switch (26), low filth switch (22), excrement inlet tube (19), heavy phase solid form exit pipe (10), heavy phase solid form discharge valve (36), deposit foul solution outlet pipe (41), deposit foul solution stop valve (42), deposit foul solution pipe (43), deposit foul solution discharge valve (44), A supernatant outlet pipe (112), a supernatant stop valve (113), a supernatant pipe (114), a supernatant pipe delivery electromagnetic valve (115), a foul solution overflow pipe (111), a foul solution return pipe (123), a second odor discharge pipe (98), a primary filter screen flushing compressed air supply pipe (184), a secondary filter screen flushing compressed air supply pipe (185), a heavy phase solid delivery pipe (37), a precipitated foul solution delivery pipe (45) and a solid pipeline collection tee joint (38); after an excrement emptying valve (18) of the excrement collecting subsystem is opened, excrement with certain pressure in the excrement collecting box (9) is directly discharged into a solid-liquid separation box (20) through an excrement inlet pipe (19), the excrement with certain pressure is separated from heavy-phase excrement and urine through twice filtration of a self-cleaning primary filter screen component (35) and a self-cleaning secondary filter screen component (32) in the solid-liquid separation box (20), solid matters with large particle sizes are remained in a solid matter cavity, solid matters with small particle sizes and black water flow into a liquid cavity and are precipitated in the liquid cavity, and the black water enters an upper clear liquid cavity; the solid substance chamber, the liquid chamber and the supernatant liquid chamber of the solid-liquid separation box (20) are designed into V-shaped structures with wide upper parts and narrow lower parts, and in order to enable the solid substances in the solid substance chamber to be concentrated as soon as possible, the sliding filter plate (25) in the solid substance chamber is designed to form a certain angle with the bottom of the box body so as to be beneficial to the concentration of the solid substances; the concentrated solid matter is retained above the heavy phase solid matter outlet (24); the black water after primary filtration enters a liquid cavity and then is subjected to secondary filtration consisting of a self-cleaning secondary filter screen (32), the black water with relatively large particle size is left in the liquid cavity, the black water flows into a supernatant liquid cavity, and as the liquid cavity and the supernatant liquid cavity are both designed into V-shaped structures with wide upper parts and narrow lower parts, a dirt collecting box (9) is emptied, a dirt emptying valve (18) is closed and the primary filtration is basically finished, the flowability of the black water is weakened, flocculent solids with certain particle size are slowly precipitated at the lower part of the liquid cavity, and the black water is used as supernatant liquid and is left at the upper parts of the liquid cavity and the supernatant liquid cavity; the self-cleaning primary filter screen component (35) and the self-cleaning secondary filter screen component (32) are both designed into special meshes and box structures so as to improve the filtering efficiency of the solid-liquid separation system:

a: when the dirt in the solid-state cavity is lower than the low-dirt switch (22) and before the dirt is discharged from the dirt collecting box (9), the intelligent electric control system (172) sends a primary filter screen cleaning instruction to the air-water control device (177), and the self-cleaning primary filter screen assembly (350) is purged and cleaned by constant-pressure high-pressure air through the primary filter screen flushing compressed air supply pipe (184) to prepare for next solid-liquid separation;

b: when the black water in the liquid cavity is lower than the low liquid level switch (26), the intelligent electric control system (172) sends an instruction for cleaning the secondary filter screen to the air-water control device (177), and the compressed air supply pipe (185) is flushed through the secondary filter screen to supply constant-pressure high-pressure air to the self-cleaning secondary filter screen assembly (32) for blowing and cleaning so as to prepare for next solid-liquid separation; when the excrement evacuation valve (18) is closed for a certain time, the supernatant pipe is conveyed to the electromagnetic valve (115) to be opened, the first electric booster pump (117) works, and the pressurized supernatant with a certain pressure is conveyed to the electrodeless photocatalytic treatment urine treatment subsystem for treatment through the heat exchanger (147); when a low liquid level switch (26) of the solid-liquid separation subsystem detects that the liquid level is low, the low liquid level switch (26) acts, and a first electric booster pump (117) of the heat exchange subsystem stops working; the sewage precipitation stop valve (42) and the supernatant stop valve (113) are opened when the solid-liquid separation subsystem normally works, and are manually opened to closed positions only when the system is overhauled or has a fault; in the process that the black water in the liquid cavity and the supernatant cavity of the solid-liquid separation box (20) is sent to the electrodeless photocatalytic treatment urine treatment subsystem for treatment, the semi-liquid level switch (47) is actuated along with the reduction of the liquid level, then a third drain valve control air pipe (183) controlled by an air-water control device (177) opens a heavy-phase solid matter discharge valve (36), solid matters reserved above a heavy-phase solid matter outlet (24) are conveyed to a sewage pump (40) with a reamer of a microwave incineration subsystem through the heavy-phase solid matter discharge valve (36), a heavy-phase solid matter conveying pipe (37), a solid matter pipeline collecting tee joint (38) and a solid matter conveying pipe (39) to be reamed and conveyed until the solid matters fall to the detection position of a low-dirt switch (22), the low-dirt switch (22) is actuated, all solid in the solid cavity is discharged, and then the heavy-phase solid discharge valve (36) is closed; at the stage, the excrement emptying valve (18) is always in a closed state until the self-cleaning primary filter screen assembly (35) finishes self-cleaning, so that the next emptying of the sewage collecting box (9) is allowed; a certain amount of black water is stored at the lower part of the sliding filter plate (25) and is used for ensuring the proper fluidity of solid matters;

after solid matters in the solid matter cavity are emptied and the heavy phase solid matter discharge valve (36) is closed, the precipitated sewage discharge valve (44) is opened, the precipitates in the liquid cavity are conveyed to a sewage pump (40) with a reamer of a microwave incineration subsystem through a precipitated sewage conveying pipe (45) and a solid matter pipeline collecting tee joint (38) under the action of gravity to be properly cleaned, and meanwhile, the precipitated pollutants which are not suitable for being conveyed to the urine treatment subsystem without the extreme photocatalysis treatment are conveyed to the microwave incineration subsystem; the odor in the solid-liquid separation box (20) is sent into the electrodeless photocatalytic treatment waste gas treatment subsystem for decomposing the odor through a first odor outlet (31), a second odor outlet pipe (98), a first odor pipeline tee joint (155), a third odor delivery pipe (99), a second odor pipeline tee joint (156) and a fourth odor delivery pipe (100) through an axial flow fan (102) of the electrodeless photocatalytic treatment waste gas treatment subsystem; the black water which is not treated by the urine treatment subsystem of the electrodeless photocatalysis treatment is temporarily discharged into a residual liquid box (124) for temporary storage through a waste liquid overflow outlet (29) and a waste liquid overflow pipe (111).

5. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the microwave incineration subsystem comprises: the device comprises a sewage pump (40) with a reamer, a coarse pulp box (49), an electric crusher (54), a fine pulp box (56), a first self-sucking pump (61), a fine pulp preheating box (63), a first stop valve (83), a second self-sucking pump (85), an incineration electric valve (89) and a microwave incinerator (71); wherein:

A. the coarse pulp box (49) is provided with a coarse pulp receiving port (48), a second coarse pulp conveying pipe (53), a second full liquid level sensor (51), a first low liquid level sensor (52), a second odor outlet (50) and a first coarse pulp conveying pipe (46);

a sewage pump (40) with a reamer reams solid matters and sediments sent by a solid-liquid separation subsystem, and sends the crushed solid matters and sediments into a coarse pulp box (49) through a first coarse pulp conveying pipe (46), when certain coarse pulp exists in the coarse pulp box (49), a first low liquid level sensor (52) acts, and the coarse pulp flows into an electric crusher (54) through a second coarse pulp conveying pipe (53) and starts to work;

the odor generated in the coarse pulp box (49) passes through a second odor outlet (50), a first odor delivery pipe (94), an odor tee joint (154), a second odor delivery pipe (97), a first odor pipeline tee joint (155), a third odor delivery pipe (99), a second odor pipeline tee joint (156), a fourth odor delivery pipe (100) and an axial flow fan (102) of the electrodeless photocatalytic waste gas treatment subsystem to be delivered into the electrodeless photocatalytic waste gas treatment subsystem for decomposing the odor;

a second full liquid level sensor (51) of the coarse slurry tank (49) is used for alarming that the coarse slurry tank (49) is full;

B. the receiving port of the electric crusher (54) is directly communicated with the coarse pulp box (49) through a second coarse pulp conveying pipe (53) to receive coarse pulp flowing into the coarse pulp box (49), the coarse pulp is further crushed and ground after the electric crusher is started, and the coarse pulp is conveyed into the fine pulp box (56) through a first fine pulp conveying pipe (55) for transfer;

C. the fine pulp box (56) is provided with a first fine pulp conveying pipe (55), a first fine pulp output port (59), a third full liquid level sensor (57), a second low liquid level sensor (58) and a first fine pulp output pipe (60);

the fine pulp crushed and ground by the electric crusher (54) directly falls into a fine pulp box (56) by gravity and flows into a first self-sucking pump (61) through a first fine pulp output port (59) and a first fine pulp output pipe (60);

when the fine pulp tank (56) is filled with fine pulp, the third full liquid level sensor (57) acts, the first self-sucking pump (61) is started to pump the fine pulp into the fine pulp preheating tank (63), after the first self-sucking pump (61) works, the fine pulp in the fine pulp tank (56) is gradually reduced, when the level of the fine pulp is low to touch the second low liquid level sensor (58) to act, the first self-sucking pump (61) stops working, and the fine pulp in the fine pulp tank (56) is completely transferred to the fine pulp preheating tank (63);

a third full liquid level sensor (57) of the fine pulp tank (56) is used for alarming when the fine pulp tank (56) is full and controlling the starting of the first self-priming pump 61;

D. the fine pulp preheating box (63) is provided with a fine pulp inlet (67), a flue (76), a flue opening (77), a third odor outlet (96), a second fine pulp outlet (75), a flue gas inlet pipe (70), a fourth full level sensor (64), a semi-liquid level sensor (65), a third low level sensor (66), an annular heater (69), a temperature control sensor (68), a second fine pulp conveying pipe (62), a first odor outlet pipe (95), a flue gas outlet pipe (107), a second fine pulp output pipe (82), a first stop valve (83), a third fine pulp conveying pipe (84), a second self-priming pump (85), a fourth fine pulp conveying pipe (86), a second tee joint (87), a fifth fine pulp conveying pipe (88), an incineration electric valve (89) and a fine pulp input pipe (90);

the fine pulp sucked by the first self-sucking pump (61) from the fine pulp box (56) is sent into the fine pulp preheating box (63) through the second fine pulp conveying pipe (62) and the fine pulp inlet (67), when the liquid level of the fine pulp is higher than that of the third low liquid level sensor (66), the third low liquid level sensor (66) acts, the annular heater (69) starts to work, and the temperature control sensor (68) is used for detecting the temperature of the fine pulp and controlling the work of the annular heater (69) through the intelligent control system;

when the microwave incinerator (71) is not operated and the fine slurry is pumped from the fine slurry tank (56) to the fine slurry preheating tank (63), the annular heater (69) is mainly electrified to work to preheat the fine slurry, after the microwave incinerator (71) is operated, high-temperature hot steam and high-temperature waste gas after solid incineration simultaneously heat the fine slurry through a flue (76) in the fine slurry preheating tank (63), when the temperature of the fine slurry reaches a preset temperature, the intelligent control system sends out a stop instruction of the annular heater (69) to stop the operation of the annular heater, and then the fine slurry is completely preheated through the high-temperature hot steam after solid incineration and the high-temperature waste gas after combustion;

after the first self-sucking pump (61) is started, the fine pulp sucked from the fine pulp box (56) is sent into a fine pulp preheating box (63) through a second fine pulp conveying pipe (62) and a fine pulp inlet (67), when the level of the fine pulp is higher than a half liquid level sensor (65) and the fine pulp reaches a preset temperature, a second self-sucking pump (85) is started, and the preheated fine pulp is sent to an atomizing nozzle input port (74) of a microwave incinerator (71) through a second fine pulp output port (75), a second fine pulp output pipe (82), a first stop valve (83), a third fine pulp conveying pipe (84), a second self-sucking pump (85), a fourth fine pulp conveying pipe (86), a second tee joint (87), a fifth fine pulp conveying pipe (88), an incinerating electric valve (89) and a fine pulp input pipe (90);

after the microwave incinerator (71) works, high-temperature hot steam generated after solid matter incineration treatment and high-temperature waste gas after combustion preheat fine slurry through a flue (76) in a fine slurry preheating box (63), the high-temperature hot steam is mixed with high-temperature hot steam discharged by the urine treatment subsystem without the extreme light catalytic treatment through a flue port (77), a flue gas discharge pipe (107) through a third tee joint (108), and then the mixture is conveyed to a heat exchanger (147) through a high-temperature gas conveying pipe (109) to preheat black water conveyed to the urine treatment subsystem without the extreme light catalytic treatment;

E. the microwave incinerator (71) is provided with an atomizing nozzle input port (74), a first compressed air input port (73), an ash residue discharge port (72) and a flue gas inlet pipe (70);

after being pressurized by a second self-sucking pump (85), the fine slurry preheated by the fine slurry preheating box (63) is sent to an atomizing nozzle of a microwave incinerator (71), atomization and drying treatment are carried out in the microwave incinerator (71), incineration is carried out in an incineration area, and incinerated ash residues are temporarily stored above an ash residue discharge port (72) and are cleaned and discharged when being discharged in a conditional mode;

the air-water control device (177) feeds fresh air with certain pressure into the microwave incinerator (71) through a compressed air conveying pipe (78), a first tee joint (79), a microwave incinerator air inlet pipe (80) and a first compressed air inlet (73), so that on one hand, the fresh air is used for supporting combustion, and on the other hand, solid matters dried in a drying area of the microwave incinerator can be stirred to be fully combusted; in addition, the compressed air blows high-temperature hot steam generated in the microwave incinerator (71) and high-temperature waste gas after combustion into the fine pulp preheating box (63) through the flue gas inlet pipe (70) to preheat the fine pulp.

6. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the system for processing the urine by the electrodeless photocatalysis comprises: urine processing apparatus (132), supernatant input tube (118), compressed air input tube (81), waste liquid discharge pipe (120), high temperature steam discharge port (133) are handled to electrodeless photocatalysis, wherein be equipped with on urine processing apparatus (132) of electrodeless photocatalysis: an atomizing nozzle (135), a supernatant liquid input port (134), a second compressed air input port (137), a waste liquid discharge port (136) and a high-temperature steam discharge port (133);

the electrodeless photocatalytic treatment urine treatment subsystem is also provided with a set of residual liquid storage device, which comprises a residual liquid tank (124), a solid-liquid separation subsystem overflow liquid discharge port (127), an electrodeless photocatalytic treatment urine treatment subsystem unprocessed supernatant liquid discharge port (128), a system cleaning dirty liquid discharge port (129), a residual liquid tank cleaning drain outlet (131), a residual liquid output port (126), a first residual liquid conveying pipe (121), a second electric booster pump (122), a cleaning sewage conveying pipe (91), a flushing dirty liquid electric valve (92), a drain pipe (196), a second stop valve (197), a fifth full liquid level sensor (125) and a fourth low liquid level sensor (130);

when the feces evacuation valve (18) is closed for a certain time, the electrodeless photocatalytic treatment urine treatment device is started to preheat, a supernatant pipe in the solid-liquid separation device is conveyed to the electromagnetic valve (115) to be opened, a first electric booster pump (117) of the heat exchange subsystem works, and the pressurized supernatant with a certain pressure is conveyed to an atomizing nozzle (135) of the electrodeless photocatalytic treatment urine treatment device through a supernatant input pipe (118), a heat exchanger (147) and a supernatant input port (134) to be subjected to microwave electrodeless photocatalytic degradation sterilization treatment;

the high-temperature steam that produces among the supernatant degradation treatment process sends into heat exchange system for supernatant input system heating through the pressure air that the wind regime system sent into and the high-temperature flue gas that the microwave incineration system produced together, and the delivery path of high-temperature steam is in proper order: a urine treatment device (132) for electrodeless photocatalytic treatment, a high-temperature steam outlet (133), a third tee joint (108), a high-temperature gas delivery pipe (109) and a heat exchanger (147);

the air-water control device (177) sends fresh air with certain pressure to the electrodeless photocatalytic treatment urine treatment device (132) through the compressed air conveying pipe (78), the first tee joint (79), the compressed air input pipe (81) and the second compressed air input port (137), on one hand, atomized liquid sprayed out of an atomizing nozzle (135) of the electrodeless photocatalytic treatment urine treatment device (132) can be stirred to be fully degraded, on the other hand, the degraded high-temperature water vapor is promoted to be discharged, and the circulation of the water vapor is facilitated;

because the supernatant is not fully preheated in the starting process of the electrodeless photocatalytic treatment urine treatment device (132) and the microwave incineration system, part of atomized water still falls to a liquid collecting area at the lower part of the electrodeless photocatalytic treatment urine treatment device (132) in the form of the supernatant, and is sent back to the residual liquid tank (124) through a waste liquid discharge port (136) and a waste liquid discharge pipe (120) of the electrodeless photocatalytic treatment urine treatment device (132) and finally returned to a supernatant cavity of the solid-liquid separation system;

the raffinate tank (124) collects and stores:

A. the supernatant fluid overflowed by the solid-liquid separation system has the following path: the solid-liquid separation tank (20), a sewage overflow outlet (29), a sewage overflow pipe (111), and an overflow discharge inlet (127) of the solid-liquid separation subsystem are discharged into a residual liquid tank (124) for temporary storage;

B. part of atomized water of the urine treatment device (132) for the electrodeless photocatalytic treatment falls to a lower liquid collecting area of the urine treatment device (132) for the electrodeless photocatalytic treatment in the form of supernatant, and is sent back to the residual liquid tank (124) through a waste liquid discharge port (136), a waste liquid discharge pipe (120) and an untreated supernatant discharge port (128) of the urine treatment device (132) for the electrodeless photocatalytic treatment;

C. returning system washing water: sewage generated in the system flushing process is discharged by the fine slurry preheating box and then is sent to the residual liquid box (124) through a second fine slurry output port (75), a second fine slurry output pipe (82), a first stop valve (83), a third fine slurry conveying pipe (84), a second self-sucking pump (85), a fourth fine slurry conveying pipe (86), a second tee joint (87), a cleaning sewage conveying pipe (91), a flushing sewage electric valve (92), a flushing sewage conveying pipe (93) and a system cleaning sewage discharge port (129);

dirty liquid stored in the residual liquid tank (124) is sent into a liquid cavity of the solid-liquid separation device (20) through a second electric booster pump (122), and the conveying path is as follows:

a residual liquid tank (124), a residual liquid outlet (126), a first residual liquid conveying pipe (121), a second electric booster pump (122), a cleaning dirty liquid conveying pipe (93) and a dirty liquid return inlet (30) return to a liquid cavity of the solid-liquid separation device (20); the start of the second electric booster pump (122) is controlled by a fifth full liquid level sensor (125), when the second electric booster pump (122) is started, the raffinate is pumped to reduce the liquid level of the raffinate tank (124), and when a fourth low liquid level sensor (130) acts, the second electric booster pump (122) stops working;

if the residual liquid tank (124) needs to be cleaned or the whole system needs to be stopped, the dirty liquid in the residual liquid tank (124) can be completely drained, and the process is as follows:

when the second stop valve (197) is opened, dirty liquid in the residual liquid tank (124) is discharged through the residual liquid tank cleaning sewage outlet (131), the second stop valve (197), the second residual liquid conveying pipe (198), the four-way joint (146), the fifth drain pipe (193) and the drain joint (194); the drainage joint (194) adopts a special fire-fighting pipe joint for a fire-fighting system.

7. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the electrodeless photocatalytic treatment exhaust gas treatment subsystem comprises: the device comprises an electrodeless photocatalytic treatment waste gas treatment device (105), an axial flow fan (102), a waste gas input pipe (103), a waste gas input port (104) and a clean gas discharge port (106); the odor of the solid-liquid separation subsystem and the microwave incineration subsystem and the high-temperature steam and the smoke which are generated by the heat-exchanged electrodeless photocatalytic treatment urine treatment subsystem and are not completely liquefied are sent into an electrodeless photocatalytic treatment waste gas treatment device (105) through an axial flow fan (102), a waste gas input pipe (103) and a waste gas input port (104) to be subjected to photochemical reaction to carry out deodorization and degradation treatment on organic gas and then are discharged from a clean gas discharge port (106).

8. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the heat exchange sub-system comprises: the device comprises a heat exchanger (147), a high-temperature flue gas inlet (149), a flue gas outlet (148), a supernatant inlet (150), a high-temperature supernatant outlet (151), a second reclaimed water outlet (152), a high-temperature gas delivery pipe (109), a flue gas output pipe (101), a supernatant input pipe (118), a high-temperature supernatant input pipe (119), a first reclaimed water output pipe (153) and a first electric booster pump (117); after the microwave incinerator (71) works, high-temperature hot steam generated after solid material incineration treatment and high-temperature waste gas after combustion preheat fine slurry through a flue (76) in a fine slurry preheating box (63), and are mixed with a high-temperature hot steam output pipe (110) discharged by the urine treatment subsystem of the electrodeless photocatalytic treatment through a third tee joint (108) through a flue opening (77) and a flue gas discharge pipe (107), then the black water sent to the electrodeless photocatalytic treatment urine treatment subsystem is sent to a heat exchanger (147) through a high-temperature gas conveying pipe (109) and a high-temperature flue gas inlet (149) to carry out heat exchange on the black water, then the black water is mixed with odor through a flue gas outlet (148), a flue gas output pipe (101) and a second odor pipeline tee joint (156), and then the mixture is sent to the electrodeless photocatalytic treatment waste gas treatment subsystem through an axial flow fan (102) to carry out odor removal and degradation treatment on organic gas, and then the organic gas is discharged from a clean gas outlet (106); when the feces evacuation valve (18) is closed for a certain time, the electrodeless photocatalytic treatment urine treatment device is started to preheat, a supernatant pipe in the solid-liquid separation device is conveyed to the electromagnetic valve (115) to be opened, a first electric booster pump (117) of the heat exchange subsystem works to lead supernatant to be discharged from the solid-liquid separation box (20), a supernatant outlet (28), a supernatant outlet pipe (112), a supernatant stop valve (113) and a supernatant pipe (114), a supernatant fluid delivery electromagnetic valve (115), a supernatant fluid delivery pipe (116), a first electric booster pump (117) and a supernatant fluid input pipe (118) are pressurized, then sent into a heat exchanger (147) for heat exchange and temperature rise, and then delivered to an atomizing nozzle (135) of the urine treatment device for electrodeless photocatalytic degradation and sterilization treatment through a high-temperature supernatant fluid input pipe (119) and a supernatant fluid input port (134); high-temperature hot steam generated by a microwave incinerator, high-temperature waste gas after combustion and high-temperature hot steam discharged by an electrodeless photocatalytic treatment urine treatment subsystem exchange heat with normal-temperature supernatant liquid output by a solid-liquid separation box (20) in a heat exchanger (147), moisture in the high-temperature hot steam is condensed and washed out to generate reclaimed water, the reclaimed water falls into a hopper-shaped reclaimed water storage area at the lower part of the heat exchanger, and then the reclaimed water falls into a reclaimed water tank (138) through a first reclaimed water output pipe (153) to be stored for preparing for reclaimed water recycling; the flue gas after heat exchange in the heat exchanger (147) is sent to the waste gas treatment subsystem for electrodeless photocatalytic treatment for decomposition treatment of the odor through a flue gas outlet (148) of the heat exchanger, a flue gas output pipe (101), a second odor pipeline tee joint (156) and a fourth odor delivery pipe (100) through an axial flow fan (102) of the waste gas treatment subsystem for electrodeless photocatalytic treatment.

9. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the recycled water recycling toilet flushing subsystem comprises: well water tank (138), clear water tank (157), wherein:

A. the middle water tank (138) is provided with: the water level control device comprises a reclaimed water inlet (139), a first reclaimed water outlet (142), a first overflow port (140), a first drain port (145), a sixth full liquid level sensor (141), a fifth low liquid level sensor (143), a reclaimed water pump (166), a second reclaimed water output pipe (167), a third drain pipe (189), a second drain cock (190), a first overflow pipe (144), a four-way joint (146), a fifth drain pipe (193) and a drain joint (194); when reclaimed water is collected to a certain degree, a sixth full liquid level sensor (141) on the reclaimed water tank (138) acts, a reclaimed water pump (166) starts to work, and reclaimed water in the reclaimed water tank (138) is pumped into a clean water tank (157) through a first reclaimed water outlet (142), a second reclaimed water outlet pipe (167), the reclaimed water pump (166) and a reclaimed water inlet pipe (165) for flushing; when the water level of the intermediate water in the intermediate water tank (138) is reduced to the action of the fifth low liquid level sensor (143) or the water level in the clear water tank (157) is increased to trigger a seventh full liquid level sensor (158) of the clear water tank (157), the intermediate water pump (166) stops working; when the system is first used or is reused after being out of service for a period of time, the clear water tank (157) needs to be filled with clear water from the ground water source; when the middle water tank (138) is filled with the reclaimed water, the redundant reclaimed water is discharged through the first overflow port (140), the first overflow pipe (144), the four-way joint (146), the fifth drain pipe (193) and the drain joint (194); before the system is stopped, the reclaimed water in the reclaimed water tank (138) can be drained through a drainage joint (194) through a second drainage cock (190); the drainage path is as follows: the water-saving device comprises a middle water tank (138), a first water discharge opening (145), a third water discharge pipe (189), a second water discharge cock (190), a fourth water discharge pipe (191), a water discharge tee joint (192), a sixth water discharge pipe (195), a four-way joint (146), a fifth water discharge pipe (193) and a water discharge joint (194);

B. the clear water tank (157) is provided with: the device comprises a reclaimed water inlet (161), a clean water inlet (162), a water outlet (159), a second overflow port (199), a second water outlet (169), a seventh full liquid level sensor (158), a sixth low liquid level sensor (160), a clean water pipe (163), a clean water joint (164), a reclaimed water inlet pipe (165), a first water outlet pipe (186), a first water outlet cock (187), a fourth tee joint (201) and a water pipe (168); when the water tank is used for the first time or reused, the clear water tank (157) needs to be filled with clear water from a ground water source; the water filling path is as follows: a clean water joint (164), a clean water inlet (162) and a clean water tank (157); when reclaimed water is collected to a certain degree, a sixth full liquid level sensor (141) on the reclaimed water tank (138) acts, a reclaimed water pump (166) starts to work, and reclaimed water in the reclaimed water tank (138) is pumped into a clean water tank (157) through a first reclaimed water outlet (142), a second reclaimed water outlet pipe (167), the reclaimed water pump (166) and a reclaimed water inlet pipe (165) for flushing; when the clean water tank (157) is filled with reclaimed water/clean water, the redundant water is discharged through a second overflow port (199), a second overflow pipe (200), a fourth tee joint (201), a second drain pipe (188), a drain tee joint (192), a sixth drain pipe (195), a four-way joint (146), a fifth drain pipe (193) and a drain joint (194);

when the system is not used, the water in the clear water tank (157) can be drained through the drainage joint (194) through the first drainage cock (187); the drainage path is as follows: the clean water tank (157), the second water outlet (169), the first water outlet pipe (186), the first water outlet cock (187), the seventh water outlet pipe (202), the fourth tee joint (201), the second water outlet pipe (188), the water outlet tee joint (192), the sixth water outlet pipe (195), the four-way joint (146), the fifth water outlet pipe (193) and the water outlet joint (194) are discharged.

10. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the wind source subsystem comprises: an air source (170) and an air-water control device (177); wherein:

A. the air source (170) consists of a motor and a compressor, and compressed air of 10bar can be provided through a total air pipe (171);

B. the air-water control device (177) consists of an electromagnetic valve, a pressure regulating valve, a vacuum generator and a water pressurizer, can properly pressurize cleaning water for flushing a bedpan (1), vacuumizes the sewage collection box (9) through the vacuum generator, adds proper positive pressure to the sewage collection box (9), and leads compressed air to the microwave incinerator (71) and the electrodeless photocatalytic treatment urine treatment device (132).

11. The multi-lavatory mobile intelligent net gang WC system assembly of claim 1, wherein: the intelligent control subsystem includes: the intelligent electric control device (172), the electric wire cable (174), the liquid crystal display screen (175) and the peripheral control device comprise a flushing button (173), a speaker between use, a display screen between use, a communication cable (176), a sensor, a switch, a contactor and a relay; the intelligent control subsystem controls the gas, water and electricity of the whole system according to set logic and time sequence, has the functions of advertisement, entertainment, public information broadcasting and the access function of the Internet of things, and can realize remote monitoring on the whole system.

12. A sewage treatment method of a multi-toilet-station mobile intelligent net emission WC system assembly at least comprises the multi-toilet-station mobile intelligent net emission WC system assembly, and is characterized in that: the multi-toilet-seat mobile intelligent net emission WC system assembly comprises ten subsystems including a toilet seat using subsystem, a wind source subsystem, an excrement collecting subsystem, a solid-liquid separation subsystem, a microwave incineration subsystem, an electrodeless photocatalytic treatment urine processing subsystem, an electrodeless photocatalytic treatment waste gas processing subsystem, a heat exchange system, a reclaimed water recycling toilet flushing subsystem and an intelligent control subsystem, the vacuum negative pressure solid-liquid collection system composed of the toilet seat using subsystem, the wind source subsystem and the excrement collecting subsystem is utilized to quickly and efficiently collect human excrement in multiple toilet seats, the collected solid and liquid are quickly sent into the solid-liquid separation subsystem through positive pressure provided by the wind source subsystem, solid excrement and urine contain flushing water through the solid-liquid separation subsystem to carry out liquid-solid two-phase separation, the lower phase is excrement heavy phase containing urine, and the excrement heavy phase is atomized and sent into the microwave incineration subsystem to be dried and thoroughly incinerated after being crushed by high-speed blades, tail gas of the microwave incineration subsystem enters a microwave photochemical reactor of the electrodeless photocatalytic treatment waste gas treatment subsystem for degradation and deodorization for harmless treatment; the supernatant enters the urine treatment subsystem for the electrodeless photocatalytic treatment in a spraying mode, passes through the microwave photochemical reactor under the coordination of air with proper flow provided by the air source subsystem, and organic matters in the urine are degraded into tasteless low-carbon molecular compounds under the ultraviolet light catalysis action and finally mineralized into carbon dioxide and water; cooling, liquefying and recovering moisture in the exhaust gas of the electrodeless photochemical reactor through the heat exchange system, and sending the moisture into a reclaimed water storage tank of the reclaimed water recycling toilet flushing subsystem for recycling use in toilet flushing; the intelligent control subsystem provides functions of automatic liquid level detection, automatic emission detection, gas-water electric control, human-computer interaction interface and Internet of things access; thus, an automatic control flow type treatment line for flushing the toilet by collecting excrement, separating solid from liquid, incinerating solid, atomizing urine, degrading by photocatalytic oxidation to mineralize and recycling mineralized water is sequentially formed.

Technical Field

The invention belongs to the technical field of manufacturing and application of environment-friendly energy-saving, regeneration, human excrement treatment and sewage treatment equipment in specific places including mobile or fixed places, in particular to a rapid harmless treatment system or device for cleaning, colorlessness, tastelessness, no secondary pollution and no trace up-to-standard discharge of multi-toilet-place human excrement, sewage and malodorous gas used in places such as carrying vehicles, tourist attractions, large indoor and outdoor meeting places, emergent public health event areas, urban streets, squares, parks, factories and mines, oil fields, military camps, field operation places, stations, wharfs, communities and the like; the invention can also be used in the technical field of kitchen waste treatment; the invention also relates to a method for treating the dirt generated by the WC system.

Background

The excretion is the normal physiological requirement of human beings, and the daily activities of everyone such as defecation are essential, therefore, the lavatory is an essential important facility for ensuring the sanitation and convenience of human beings, plays an important role in the daily life of people, and is not only a passenger vehicle, but also a tourist attraction, or indoor and outdoor large-scale meeting places, city streets, squares, parks, factories and mines, oil fields, field operation places, stations, docks and districts, even special places such as public health incident areas and military camps, and a certain number of toilets are required for facilitating the excretion requirement of people.

If the 'open pit' is a great progress of human civilization from the location of the ancient times to the later fixed convenient place, the 'qualitative leap' of the toilet is not found in 1597, but the toilet flushed by water designed by the English man John Harlington, and the first modern toilet patent is invented until 1775. In the following hundreds of years, a lot of English people are continuously improved, advanced water storage and flushing systems and U-shaped pipelines for preventing odor from overflowing are invented, the designs are still used up to now, but at the moment, the problem of the flow direction of sewage is not solved, most of excrement is directly discharged into rivers along the pipelines, serious environmental pollution and pathogen transmission are caused, and so that 1858 summer, the London Thames rivers burst out famous 'big odor events'. Until 1861, plumbing thomas krappe continued to improve toilets, creating more advantageous water-saving flush systems. With the development of the era and the progress of science and technology, the toilet bowl also starts to integrate more and more scientific and technological elements after the time comes to the intelligent era, but in terms of the current technical development achievements, the actual functions of the toilet bowl, whether being a single intelligent toilet bowl or a public intelligent environment-friendly toilet, are only limited to the simple collection of human excrement and the flushing of the toilet bowl, and the excrement is finally discharged into a municipal pipe network and a sewage treatment plant for centralized treatment.

Technical current situation of toilet of passenger train and high-speed rail motor train unit

For a long time, the gravity direct-discharge toilet is used by railway passenger trains, and pollutes the environment along the railway. With the increase of the running speed of trains, in order to ensure the running safety of the trains and improve the environment along the railway, a plurality of developed countries in the world try to install the closed toilets from the last 60 years to a large number of excrement collectors from the seventy years. In China, high-speed rail and passenger special lines are built into a common train in sequence from 2007, and a large number of running motor train units are provided with closed toilets. In order to further improve the environment along the railway, the closed toilets are gradually added to the ordinary speed trains according to the original railway ministry of 'railway passenger train closed toilet transformation planning'.

From the current application, the main types of closed toilets used in passenger trains and high-speed trains are vacuum-holding toilet collectors, compact vacuum toilet collectors, circulating toilet collectors, and pressure-flushing toilet collectors. The water circulation type excrement collecting device in the united states, the EVAC vacuum excrement collecting device in sweden, the temporary excrement collecting device in korea and the Monogram vacuum excrement collecting device in the united states are used successively in China since the last 90 th century, the japanese pressurized flush water excrement collecting device is also adopted in the CRH2 type high-speed railway motor train unit passenger car designed and manufactured in China at present, and the german temporary vacuum excrement collecting device is adopted in the CRH3 type high-speed railway motor train unit passenger car.

The excrement collector for passenger trains and high-speed railway motor train units in China or abroad only has the function of collecting excrement, and is not treated after being collected on the trains, so that excrement sewage collected on the trains is only discharged into an excrement collecting box through a sewage discharge vehicle or fixed emptying equipment matched with the ground and used for the whole trains at fixed stations, passenger stations, vehicle sections and the like, and the sewage is directly sent to a municipal sewage treatment plant through the sewage discharge vehicle or is simply treated through a local septic tank or an anaerobic tank at the station sections and then discharged into a municipal sewage pipe network.

The wastewater of the excrement collector has high organic matter concentration, ammonia nitrogen concentration and SS, so the treatment difficulty is high. According to the national environmental protection requirement, the water discharged into the municipal pipe network meets CJ 343-2010 quality standard for sewage discharged into town sewers, and if the water is required to meet the requirement, a dilution method is adopted in addition to the corresponding biological treatment method, so that the required water quantity is larger. In addition, urban sewage treatment facilities in China are not developed completely, corresponding urban pipe networks do not exist around a plurality of vehicle sections, the urban pipe networks are discharged, the required pipe network investment is high, and the quantity of the stored fecal sewage is limited. The sewage discharge truck is adopted to be delivered to a municipal sewage treatment plant, and the working capacity can not meet the requirement of railway operation.

Second, the current technical situation of aviation toilet

In the four and fifty years of the 20 th century, airliner toilets were straight-through to the outside and therefore also belong to the category of direct-discharge toilets, and in the case where this did not last too long, chemical toilet technology was applied to airliner toilets, which was the beginning of modern airliner toilet technology, and consequently with the development of technology airliners used circulating toilets, but three civil airliner manufacturers (boeing, avenue and european airbus) in the world today stipulated that new aircraft after 1987 have all been retrofitted to vacuum toilet sinks. The structure of the aviation excrement collecting device is basically the same as that of an excrement collecting device of a passenger train or a high-speed rail motor train unit, but the requirement that the volume of a dirt box is facing towards the aviation passenger plane is higher.

The aviation toilet still only has the function of collecting excrement like a closed toilet of a passenger train and a high-speed rail motor train unit, and the excrement can be kept in the closed toilet until the plane lands on the ground and is cleared by ground workers in the whole flying process (the sewage is generally directly sent to a municipal sewage treatment plant by a sewage discharge vehicle, and a large airport is generally provided with a local septic tank or an anaerobic tank for simple treatment and then is discharged into a municipal sewage pipe network). Therefore, the aviation excrement collecting device has the same defects as the excrement collecting device of passenger trains and high-speed rail motor train units.

Three, vehicle trailer type mobile toilet

The vehicle-mounted trailer type mobile toilet generally has the following types: the water flushing straight discharge type toilet, the automatic packing type toilet, the foam plugging type toilet, the ecological environment protection type toilet, the micro water flushing type toilet, the vacuum adsorption type toilet, the high-pressure gas water flushing and the like are basically all in the form of a closed excrement collection toilet, some toilets are subjected to simple solid-liquid separation, a higher-level ecological environment protection type toilet is characterized in that excrement is separated and then discharged into a fermentation tank, initial ingredients, wood dust, biological strains and excrement are mixed through rotation of a spiral propeller, the mixture is decomposed under the action of microbial bacteria and separated in the form of carbon dioxide and water, urine is filtered and then enters a urine comprehensive treatment system, and the urine is treated into reclaimed water for flushing the urinal through the processes of aeration, evaporation, decoloration and the like, so that circulation is formed, the treatment period is longer, and in addition, auxiliary materials such as. Most vehicle-mounted trailer-type mobile toilets still need to be manually discharged and then sent to a municipal sewage treatment plant, or are simply treated by a septic tank or an anaerobic tank and then discharged into a municipal sewage pipe network.

Four, ground fixed type environment protection toilet

At present in park, square, the basic type and the on-vehicle trailer type mobile toilet of the fixed environmental protection lavatory in ground of tourist attraction installation are the same basically, the difference is that there is the washing and the sealed function of only stool pot in the environmental protection lavatory of municipal administration blow off pipe network region installation, the excrement is direct to the municipal administration blow off pipe network of arranging, to not having the municipal pipe network condition, set up and store up the excrement case, it takes out the excrement mouth to set up on the excrement case, it seals to take out excrement mouth lower part and is equipped with the butterfly valve, it reserves the mouth to store up excrement bottom portion, so that be connected with municipal administration blow off pipe network when possessing the condition. The higher-level ground ecological environment-friendly toilet has the same function as the vehicle-mounted trailer type microbial ecological mobile toilet, so that the sewage of the ground fixed type environment-friendly toilet is finally sent to a municipal sewage treatment plant or is simply treated by a septic tank or an anaerobic tank and then discharged into a municipal sewage pipe network.

To sum up, no matter at present vehicle-mounted mobile closed type toilet or ground fixed type environment-friendly toilet all have certain disadvantages, and the common problem is as follows:

1. most of human excrement is only collected, and excrement, urine and the like are not treated, so that the standard emission is not mentioned, and the method is basically indistinguishable from a traditional toilet and cannot realize zero-pollution standard emission;

2. most of excrement is not subjected to solid-liquid separation treatment, and excrement liquid coexists, so that the subsequent treatment difficulty is high;

3. the sewage tank/excrement storage tank has limited capacity, when the sewage tank/excrement storage tank is full of sewage, sewage discharge treatment must be carried out, otherwise, the toilet must be stopped, and inconvenience in use is caused;

4. a large amount of odor is discharged in the processes of suction, pollution discharge and transportation of the sewage discharge truck, and the bad influence is generated on the environment, so that the problems of local pollution and safety risk still exist;

5. the sewage collected by the excrement collector is subjected to ground centralized treatment, a large amount of ground water is required to be diluted, the cost is high, and huge manpower, financial resources and material resources are required to be consumed;

6. the sewage discharge needs special equipment, the labor and equipment investment cost is high, the maintenance workload is large, in addition, the excrement and urine treatment occupies social resources, and the urban sewage and sewage treatment pressure is increased;

the environmental adaptability of the excrement collector is poor; the excrement collector is mainly applied to regions with mild and humid climates in China. For some cold areas, especially in plateau and high latitude areas, the failure rate of the excrement collector is very high, and even the use is seriously influenced; therefore, it is necessary to make an innovative design on the basis of this.

Disclosure of Invention

The invention provides a solid-liquid sewage and excrement rapid sterilization, incineration treatment and sewage treatment recycling system which solves the problems of human excrement excretion environment, disease transmission and damage to body health; namely, the invention relates to a multi-toilet-space mobile intelligent WC system assembly and a sewage treatment method thereof; the technical problem to be solved is to adopt a full physical chemistry technology, integrate excrement collection, microwave incineration, photocatalytic degradation, ultraviolet sterilization, a reclaimed water toilet flushing technology and an intelligent control system into a whole, realize the quick harmless treatment of human excrement, achieve the discharge standard reaching the discharge requirements of no color, no odor and no secondary pollution, and meet the requirements of the current domestic standards of each pollutant discharge standard. The system meets the clean emission requirements of remote mobile passenger vehicles, tourist attractions, large-scale gatherings, emergent public health events and the like, and has the characteristics of mobility, low noise, low energy consumption, wide application environment range and no limitation by regions and weather conditions.

The invention aims to provide a multi-toilet-station mobile intelligent WC system assembly which can prevent the propagation of germs from the source, solve the problem of excrement pollution and realize traceless and standard-reaching discharge.

The invention also aims to provide a multi-toilet-station mobile intelligent clean-discharge WC system assembly which intelligently collects and processes human excrement and realizes ecological water-saving zero-emission pollution-free integrated high-tech of the mobile toilet.

Still another object of the present invention is to provide a method for treating sewage in a multi-toilet mobile intelligent WC system assembly.

According to the above object of the present invention, the technical solution of the present invention is as follows:

firstly, provide a many toilet seats remove intelligence net row WC system assembly, its characterized in that: the system comprises ten subsystems, namely a toilet seat using subsystem, a wind source subsystem, an excrement collecting subsystem, a solid-liquid separation subsystem, a microwave incineration subsystem, an electrodeless photocatalytic treatment urine treatment subsystem, an electrodeless photocatalytic treatment waste gas treatment subsystem, a heat exchange system, a reclaimed water recycling toilet flushing subsystem and an intelligent control subsystem;

the toilet seat using subsystem: comprises a multi-toilet-room man-machine interface, which receives human excrement and has a self-cleaning function;

the wind source subsystem: the system provides proper compressed air for the whole system and performs storage, pressure regulation, air path control and pressure air delivery of the compressed air;

the feces collection subsystem: collecting excrement received by a human-computer interface of a plurality of toilet positions through vacuum negative pressure, and sending the collected excrement to a solid-liquid separation subsystem through positive pressure;

the solid-liquid separation subsystem: carrying out solid and liquid two-phase separation treatment on human excrement; inputting the upper layer urine into a microwave photocatalytic reaction system; the lower heavy phase is atomized and enters a microwave incineration system after being cut and crushed;

the microwave incineration subsystem: after heavy phase at the lower layer of the solid-liquid separation subsystem is atomized, the heavy phase is adsorbed by SiC in the microwave incineration subsystem for incineration treatment;

the system comprises an electrodeless photocatalytic treatment urine treatment subsystem: the upper urine separated by the solid-liquid separation subsystem is atomized by a nozzle and then sprayed into a microwave photochemical reactor (liquid) for degradation and sterilization treatment, and the treated exhaust gas enters a heat exchange subsystem to cool and liquefy the moisture in the exhaust gas for toilet flushing water; the purified tail gas is exhausted after passing through a photochemical reactor;

the electrodeless photocatalytic treatment waste gas treatment subsystem: gases which are not liquefied in the microwave electrodeless photoreactor (liquid) and the tail gas of the microwave incineration system enter the electrodeless photochemical reactor (gas) to be subjected to deodorization and organic gas degradation treatment, so that the safe and odorless emission standard is achieved;

the heat exchange system is as follows: wind energy is utilized in a multi-row pipe mode to cool, liquefy and recover moisture in the exhaust gas of the electrodeless photochemical reactor (liquid), and the exhaust gas is sent to a reclaimed water recycling toilet flushing subsystem;

the recycled water recycling toilet flushing subsystem comprises: storing the water condensed and liquefied by the heat exchanger into a reclaimed water storage tank for flushing a toilet for recycling;

the intelligent control subsystem: the system provides the functions of automatic liquid level detection, automatic emission detection, gas-water electric control, human-computer interaction interface and Internet of things access for the whole system. Is the core and key of the whole system.

In addition, a sewage treatment method of the multi-toilet-space mobile intelligent net emission WC system assembly is provided, the multi-toilet-space mobile intelligent net emission WC system assembly is included, and the sewage treatment method is characterized in that: the method comprises the steps of utilizing a vacuum negative-pressure solid-liquid (solid excrement, urine and flushing water) collection system of the multi-toilet-position mobile intelligent clean-discharge WC system assembly to quickly and efficiently collect human excrement (solid liquid) of the multi-toilet positions, enabling the collected solid liquid to be quickly sent into a solid-liquid separation system through positive pressure, enabling the solid excrement and the urine (containing the flushing water) to be subjected to liquid-solid two-phase separation through the solid-liquid separation system, enabling the lower phase to be an excrement heavy phase containing urine, smashing the excrement heavy phase through a high-speed paddle, then atomizing and sending the smashed excrement heavy phase into a microwave incineration system for drying and thorough incineration, and enabling tail gas of the microwave incineration system to enter; the supernatant enters in a spraying mode, passes through a microwave photochemical reactor under the coordination of air with proper flow, and organic matters in the urine are degraded into tasteless other products under the catalysis of ultraviolet light, even mineralized into carbon dioxide and water; wherein, the water in the exhaust gas is liquefied into condensed water in the heat exchanger and collected in the reclaimed water storage tank; thereby sequentially forming an automatic control flow type treatment line from excrement collection, solid-liquid separation, solid incineration, urine atomization and photocatalytic oxidative degradation to mineralization; is a water-saving, intelligent and humanized environment-friendly technology in the true sense.

Compared with the prior art, the invention has the advantages that:

1. the pollution problem of human excrement in places such as mobile carrying tools, large-scale meeting places, emergent sanitary public events and the like is fundamentally solved by adopting the sewage treatment technology comprising a microwave electrodeless photocatalysis technology and a microwave incineration technology, the excrement can be immediately collected and completely treated in a closed manner on the spot after being discharged, germs and viruses are thoroughly killed, the propagation and propagation possibility of the germs and the viruses is avoided, and the harmless target to human health is realized;

2. meets the national requirement on environment-friendly treatment of pollutants, and can realize zero emission of solid matters such as excrement and the like without pollution. The polluted water is treated to reach the standard, reaches the urban reclaimed water treatment standard, is recycled, saves water and can be directly discharged. The odor is treated to reach the standard, and is directly discharged without peculiar smell, so that the harmless target to the natural environment is realized;

3. the system discharges pollutants up to the standard, and can effectively reduce the pressure of an urban sewage pipe network and a sewage and sewage treatment system;

4. the system operates in a closed mode, the emission reaches the standard and is discharged, the surrounding environment is not affected, and the acceptable degree of residents is high.

5. The modular design is adopted, the size is small, the weight is light, the installation is convenient and fast, the application range is wide, the high altitude and high cold environment can be suitable, the operation cost is low, the maintenance is convenient and fast, and the cost is low. The minimum replaceable unit can be replaced on line, the maintenance period is short, and a large amount of manual maintenance cost is saved;

6. a high-tech physical and chemical treatment method is adopted, any additional treatment agent, strain and the like are not needed, manual maintenance is not needed, and the operation cost is saved; manual dirt discharge and transportation of existing passenger carrying tools and mobile toilets can be avoided, and operation cost is reduced;

7. the automatic control is realized, manual intervention is not needed, and the labor cost is saved;

8. the system can realize the function of self-cleaning in idle time without manual cleaning. No pollution and zero emission, and no manual cleaning is needed;

9. the system has the access function of the Internet of things and can realize the remote monitoring of the system.

10. The toilet seat using system has the advantages of elegant environment, functions of advertisement access, public information playing and the like, and friendly human-computer interface.

11. Can realize the functions of decentralized collection and centralized processing, and is convenient for the toilet to be flexibly arranged.

12. A large amount of capital and floor space invested for fecal treatment can be saved.

13. Can realize flexible maneuvering and traceless discharge, and is suitable for special occasions with strict maneuverability requirements, such as emergency sanitary events, army camping and battle fields, and the like.

Drawings

FIG. 1 is a connection relationship diagram of a multi-toilet-space mobile intelligent clean exhaust WC system assembly and subsystems;

FIG. 2 is a schematic view of the toilet seat using device shown in FIG. 1;

FIG. 3 is a schematic view of the dirt collection device shown in FIG. 1;

FIG. 4 is a schematic view of the solid-liquid separation tank shown in FIG. 1;

FIG. 5 is a schematic view of the headbox configuration shown in FIG. 1;

FIG. 6 is a schematic view of the headbox configuration shown in FIG. 1;

FIG. 7 is a schematic diagram of the fine slurry preheat tank configuration shown in FIG. 1;

FIG. 8 is a schematic view of the microwave incinerator shown in FIG. 1;

FIG. 9 is a schematic view of the appearance of the urine treatment device shown in FIG. 1;

FIG. 10 is a schematic view of the raffinate tank shown in FIG. 1;

FIG. 11 is a schematic external view of the heat exchanger shown in FIG. 1;

FIG. 12 is a schematic view of the tank configuration shown in FIG. 1;

FIG. 13 is a schematic external view of the electrodeless photocatalytic treatment exhaust treatment device shown in FIG. 1;

fig. 14 is a schematic view of the clean water tank shown in fig. 1.

Please refer to fig. 1 and fig. 2 to 14 for the following description:

a bedpan 1; a bedpan flushing nozzle 2; a toilet flushing water supply pipe system 3; a bedpan full level switch 4; a feces dropping port 5; a first drain pipe 6; a quick drain valve 7; a second drain pipe 8; a dirt collection box 9; a heavy phase solids outlet pipe 10; a vacuum suction port 11; a manure inlet 12; a manure outlet 13; a positive pressure air supply port 14; a first full level sensor 15; an inspection port 16; a third drain pipe 17; a fecal sewage evacuation valve 18; a fecal sewage inlet pipe 19; a solid-liquid separation tank 20; a full level switch 21; a low dirt switch 22; a manure inlet 23; a heavy phase solids outlet 24; sliding the filter plate 25; a low level switch 26; a settled sludge outlet 27; a supernatant outlet 28; a dirty liquid overflow outlet 29; the dirty liquid returns to the inlet 30; a first odor outlet port 31; a self-cleaning secondary filter screen assembly 32; the secondary filter screen flushes the compressed air supply port 33; the primary filter screen flushes the compressed air supply port 34; a self-cleaning primary filter screen assembly 35; a heavy phase solids discharge valve 36; heavy solid transport pipe 37; a solid matter pipeline collection tee 38; a solid matter delivery pipe 39; a sewage pump 40 with a reamer; a precipitation sewage outlet pipe 41; a sedimentation sewage stop valve 42; a settling sludge pipe 43; a precipitated waste liquid discharge valve 44; a conveying pipe 45 for the precipitated sewage; a first brown stock duct 46; a half level switch 47; a brown stock receiving opening 48; a coarse pulp tank 49; a second odor outlet 50; a second full level sensor 51; a first low level sensor 52; a second brown stock duct 53; an electric pulverizer 54; a first fine pulp transport pipe 55; a fine pulp tank 56; a third full level sensor 57; a second low level sensor 58; a first fine pulp outlet 59; a first fine pulp outlet pipe 60; a first self-priming pump 61; a second fine pulp transport pipe 62; a fine slurry preheating tank 63; a fourth full level sensor 64; a semi-level sensor 65; a third low level sensor 66; a fine slurry inlet 67; a temperature control sensor 68; a ring heater 69; a flue gas inlet duct 70; a microwave incinerator 71; an ash discharge port 72; a first compressed air input port 73; atomizing nozzle input port 74; a second fine slurry outlet 75; a flue 76; a flue port 77; a compressed air delivery pipe 78; a first tee 79; an air inlet pipe 80 of the microwave incinerator; a compressed air input pipe 81; a second fine pulp outlet pipe 82; a first cut-off valve 83; a third fine pulp transport pipe 84; a second self-priming pump 85; a fourth fine pulp feed pipe 86; a second tee 87; a fifth fine pulp transport pipe 88; incinerating the electric valve 89; a fine slurry inlet pipe 90; cleaning the sewage delivery pipe 91; a flushing sewage liquid electric valve 92; a sewage flushing delivery pipe 93; a first odor delivery conduit 94; a first odor outlet pipe 95; a third odor outlet 96; a second odor duct 97; a second odor outlet pipe 98; a third odor delivery conduit 99; a fourth odor delivery duct 100; a flue gas output pipe 101; an axial flow fan 102; an exhaust gas inlet pipe 103; an exhaust gas input 104; an electrodeless photocatalytic treatment exhaust gas treatment device 105; a clean gas exhaust port 106; a flue gas outlet pipe 107; a third tee 108; a high-temperature gas delivery pipe 109; a high temperature hot steam output pipe 110; a dirty liquid overflow pipe 111; a supernatant outlet pipe 112; a supernatant cut-off valve 113; a supernatant tube 114; the supernatant pipe delivers an electromagnetic valve 115; a supernatant delivery pipe 116; a first electric booster pump 117; a supernatant inlet line 118; a high temperature supernatant input pipe 119; a waste liquid discharge pipe 120; a first residual liquid delivery pipe 121; the second electric booster pump 122; the dirty liquid returns to pipe 123; a raffinate tank 124; a fifth fill level sensor 125; a raffinate outlet 126; an overflow drain 127; untreated supernatant discharge 128; a system cleaning waste liquid discharge port 129; a fourth low level sensor 130; the residual liquid tank cleaning drain 131; an electrodeless photocatalytic treatment urine disposal means 132; a high-temperature steam discharge port 133; a supernatant input port 134; an atomizing nozzle 135; a waste liquid discharge port 136; a second compressed air input port 137; a middle water tank 138; a reclaimed water inlet 139; a first overflow 140; a sixth full level sensor 141; a first reclaimed water outlet 142; a fifth low level sensor 143; a first overflow pipe 144; a first drain opening 145; a cross-joint 146; a heat exchanger 147; a flue gas outlet 148; a high temperature flue gas inlet 149; a supernatant inlet 150; a high temperature supernatant outlet 151; a second reclaimed water outlet 152; a first medium water output pipe 153; an odor tee 154; a first odor conduit tee 155; an odor line tee 156; a clear water tank 157; a seventh full level sensor 158; a water outlet 159; a sixth low level sensor 160; a reclaimed water inlet 161; a clear water inlet 162; a clear water pipe 163; a clean water connection 164; a reclaimed water inlet pipe 165; a reclaimed water pump 166; a second medium water outlet pipe 167; a water pipe 168; a second drain 169; a source of wind 170; a main air duct 171; an intelligent electronic control device 172; a flush button 173; a wire cable 174; a liquid crystal display screen 175; a communication cable 176; a gas-water control device 177; a toilet flush water pipe 178; a first bleed valve control gas line 179; a dirt collection box evacuation tube 180; a positive pressure gas-filled tube 181 of the dirt collection box; the second drain valve controls the air pipe 182; the third drain valve controls the air pipe 183; the primary filter screen washes the compressed air supply pipe 184; the secondary filter screen washes the compressed air supply pipe 185; a first drain pipe 186; a first drain plug 187; a second drain pipe 188; a third drain pipe 189; a second drain cock 190; a fourth drain pipe 191; a drain tee 192; a fifth drain pipe 193; a drain fitting 194; a sixth drain pipe 195; a blow-off pipe 196; a second stop valve 197; a second raffinate transfer line 198; a second overflow 199; a second overflow pipe 200; a fourth tee 201; a seventh drain 202.

Detailed Description

Embodiments of the present invention are described below, but should not be limited to, in conjunction with the following figures:

referring to the attached drawings of the invention, each subsystem of the multi-toilet-space mobile intelligent clean emission WC system assembly is characterized as follows:

the toilet seat uses the subsystem, includes: a bedpan 1, a bedpan washing nozzle 2 supplied with water through a bedpan washing water pipe 178 by a washing valve of an air-water control device 177, a bedpan washing water supply pipe system 3, a feces dropping opening 5, and a bedpan full level switch 4. The subsystem is a main human-computer interface, the bedpan 1 receives human excrement, after the excrement is discharged, the flushing button 173 is operated, the excrement collecting subsystem opens the quick discharge valve 7 through the first discharge valve control air pipe 179 under the control of the intelligent electric control device 172 and the air-water control device 177 of the wind source subsystem, under the action of vacuum pressure in the excrement collecting box 9, excrement is quickly sucked into the excrement collecting box 9, and when the quick discharge valve 7 is opened, the bedpan flushing water supply pipe system 3 supplies water with certain pressure, so that the bedpan flushing nozzle 2 sprays water to flush the bedpan 1;

when the bedpan 1 is full of feces, the bedpan full liquid level switch 4 outputs a bedpan flushing instruction, and the execution process of the instruction is consistent with the bedpan flushing instruction sent by the flushing button 173;

the fecal collection subsystem comprising: the rapid drain valve 7, the dirt collecting box 9 and the dirt emptying valve 18, wherein the main body of the dirt collecting box 9 is cylindrical and can bear certain negative pressure and positive pressure repeatedly, a dirt inlet 12, a dirt outlet 13, an inspection port 16, a vacuum suction port 11 connected with a dirt collecting box vacuumizing tube 180 controlled by an air-water control device 177, a positive pressure air supply port 14 connected with a dirt collecting box positive pressure inflation tube 181 controlled by the air-water control device 177, a first full liquid level sensor 15, a first drain pipe 6, a second drain pipe 8 and a third drain pipe 17 are arranged on the box body.

When the intelligent electric control device 172 detects that the toilet in the toilet use subsystem is not used by people, namely the flushing button 173 is not pressed down, the air-water control device 177 of the air source subsystem sends a vacuumizing instruction, the vacuum generator starts to work to pump the dirt collecting box 9 to a certain vacuum degree, the vacuum degree is kept in a certain range all the time, the vacuum pressure switch in the air-water control device 177 is used for controlling the upper limit value and the lower limit value (which can be set to-10 KPa to-25 KPa) of the vacuum degree range, when the vacuum degree in the dirt collecting box 9 is reduced to be below-10 KPa, the ejector automatically starts to work to pump the dirt collecting box 9 to be vacuum until the vacuum degree in the dirt collecting box 9 reaches-25 KPa, and the ejector automatically stops working. The waste collection tank 9, which is maintained at a range of vacuum pressure, provides for flushing of the bowl 1;

when the first full liquid level sensor 15 of the dirt collection box 9 detects that the collected dirt in the dirt collection box 9 is full, an instruction for emptying the dirt collection box 9 is sent to the intelligent electronic control device 172, at the moment, the flushing instruction for temporarily shielding and storing the bedpan 1 is sent, the quick drain valve 7 is kept in a closed state, meanwhile, an emptying instruction is sent to the dirt collection box 9, the dirt collection box emptying electromagnetic valve in the air-water control device 177 of the air source subsystem is made to act, 0.3MPa compressed air is provided for the dirt collection box 9, and meanwhile, the dirt emptying valve 18 is opened through the second drain valve control air pipe 182 controlled by the air-water control device 177 to force the dirt collection box 9 to be emptied; the volume of the dirt collecting box 9 is unchanged, so the emptying time of the dirt collecting box is limited, after the set time is continued, the dirt collecting box emptying electromagnetic valve and the dirt emptying valve 18 in the air-water control device 177 of the air source subsystem are simultaneously closed, the process automatically shifts to the vacuumizing program of the dirt collecting box 9, after the vacuum pressure in the dirt collecting box 9 meets the set requirement, the intelligent electric control device 172 firstly detects whether a flushing instruction of the temporarily shielded bedpan 1 exists, if so, the cleaning process of the bedpan 1 is immediately executed, if not, the flushing instruction of the bedpan 1 is shifted to be detected, and the dirt collecting box 9 is enabled to keep a vacuum negative pressure state;

the solid-liquid separation subsystem comprises: a solid-liquid separation box 20, a feces inlet 23, a heavy phase solid matter outlet 24, a precipitated feces liquid outlet 27, a supernatant liquid outlet 28, a feces liquid overflow outlet 29, a feces liquid return inlet 30, a first odor outlet 31, a self-cleaning primary filter screen assembly 35, a self-cleaning secondary filter screen assembly 32, a slide filter screen 25, a primary filter screen flushing compressed air supply port 34, a secondary filter screen flushing compressed air supply port 33, a full liquid level switch 21, a semi liquid level switch 47, a low liquid level switch 26, a low dirt switch 22, a feces dirt inlet pipe 19, a heavy phase solid matter outlet pipe 10, a heavy phase solid matter discharge valve 36, a precipitated feces liquid outlet pipe 41, a precipitated feces liquid stop valve 42, a precipitated feces liquid pipe 43, a precipitated feces liquid discharge valve 44, a supernatant liquid outlet pipe 112, a supernatant liquid stop valve 113, a supernatant liquid pipe 114, a supernatant liquid pipe delivery electromagnetic valve 115, a feces liquid overflow pipe 111, a feces liquid return pipe 123, a supernatant liquid return pipe, A second odor outlet pipe 98, a primary filter screen flushing compressed air supply pipe 184, a secondary filter screen flushing compressed air supply pipe 185, a heavy phase solid conveying pipe 37, a precipitated foul solution conveying pipe 45 and a solid pipeline collecting tee joint 38.

After an excrement emptying valve 18 of the excrement collecting subsystem is opened, excrement with certain pressure in the excrement collecting box 9 is directly discharged into a solid-liquid separation box 20 through an excrement inlet pipe 19, the excrement with certain pressure is separated from heavy-phase excrement (possibly containing certain toilet paper, other blocky/conglobate objects accidentally lost by a user and the like, hereinafter the same as the solid object for short) and urine (containing flushing water and hereinafter the black water for short) through twice filtration of a self-cleaning primary filter screen component 35 and a self-cleaning secondary filter screen component 32 in the solid-liquid separation box 20, the solid object with larger particle size is remained in a solid object cavity, the solid object with smaller particle size and the black water flow into a liquid cavity and are precipitated in the liquid cavity, and the black water enters an upper clear liquid cavity.

The solid substance chamber, the liquid chamber and the supernatant liquid chamber of the solid-liquid separation box 20 are designed into V-shaped structures with wide upper parts and narrow lower parts, and in order to enable the solid substances in the solid substance chamber to be concentrated as soon as possible, the sliding filter plate 25 in the solid substance chamber is designed to form a certain angle with the bottom of the box body so as to be beneficial to the concentration of the solid substances; the collected solids are retained above the heavy phase solids outlet 24.

The black water after the primary filtration enters the liquid cavity and then is subjected to secondary filtration of a self-cleaning secondary filter screen composition 32, the black water with relatively large particle size is left in the liquid cavity, the black water flows into the supernatant liquid cavity, the liquid cavity and the supernatant liquid cavity are both designed into V-shaped structures with wide upper parts and narrow lower parts, the sewage collecting box 9 is emptied, the excrement and sewage emptying valve 18 is closed, the flowability of the black water is weakened after the primary filtration is basically finished, flocculent solids with certain particle size are slowly precipitated at the lower part of the liquid cavity, and the black water is used as supernatant liquid and is left at the upper parts of the liquid cavity and the supernatant liquid cavity;

the self-cleaning primary filter screen component 35 and the self-cleaning secondary filter screen component 32 are both designed into special meshes and box structures so as to improve the filtering efficiency of the solid-liquid separation system:

a: when the dirt in the solid object cavity is lower than the low dirt switch 22 and before the dirt is discharged from the dirt collecting box 9, the intelligent electronic control system 172 sends a primary filter screen cleaning instruction to the air-water control device 177, and the primary filter screen washes the compressed air supply pipe 184 to supply 35 air for cleaning the primary filter screen to blow and clean by constant-pressure high-pressure air so as to prepare for next solid-liquid separation;

b: when the black water in the liquid cavity is lower than the low liquid level switch 26, the intelligent electronic control system 172 sends an instruction for cleaning the secondary filter screen to the air-water control device 177, the compressed air supply pipe 185 is flushed through the secondary filter screen to supply the self-cleaning secondary filter screen assembly 32 with constant-pressure high-pressure air for blowing and cleaning, and preparation is made for next solid-liquid separation;

when the fecal sewage emptying valve 18 is closed for a certain time, the supernatant pipe delivery electromagnetic valve 115 is opened, the first electric booster pump 117 of the heat exchange subsystem works, and the pressurized supernatant with a certain pressure is delivered to the electrodeless photocatalytic treatment urine treatment subsystem for treatment through the heat exchanger 147; when the low liquid level switch 26 of the solid-liquid separation subsystem detects that the liquid level is low, the low liquid level switch 26 is operated, and the first electric booster pump 117 of the heat exchange subsystem stops working.

The sewage precipitation stop valve 42 and the supernatant stop valve 113 are opened when the solid-liquid separation subsystem works normally, and are manually opened to closed positions only when the system is overhauled or broken down;

when the black water in the liquid cavity and the supernatant cavity of the solid-liquid separation box 20 is sent to the non-polar photocatalytic treatment urine treatment subsystem for treatment, and the semi-liquid level switch 47 is actuated along with the lowering of the liquid level, the heavy-phase solid matter discharge valve 36 is opened through the third drain valve control air pipe 183 controlled by the air-water control device 177, the solid matter collected above the heavy-phase solid matter outlet 24 is sent to the sewage pump with reamer 40 of the microwave incineration subsystem through the heavy-phase solid matter discharge valve 36, the heavy-phase solid matter delivery pipe 37, the solid matter collecting tee 38 and the solid matter delivery pipe 39 for hinging and conveying treatment, until the solid matter descends to the detection position of the low-dirt switch 22, the low-dirt switch 22 is actuated, all the solid matter in the solid matter cavity is discharged, and then the heavy-phase solid matter discharge valve 36 is closed; at this stage, the excrement emptying valve 18 is in a closed state until the self-cleaning primary filter screen assembly 35 finishes self-cleaning, so that the sewage collecting box 9 is allowed to be emptied next time;

a certain amount of black water is stored at the lower part of the sliding filter plate 25 and is used for ensuring the proper fluidity of solid matters;

after the solid matter in the solid matter cavity is emptied and the heavy phase solid matter discharge valve 36 is closed, the precipitated sewage discharge valve 44 is opened, the precipitate in the liquid cavity is sent to the sewage pump 40 with reamer of the microwave incineration subsystem through the precipitated sewage delivery pipe 45 and the solid matter pipeline collection tee 38 by the action of gravity to properly clean the sewage pump 40 with reamer, and simultaneously, the precipitated sewage which is not suitable for being sent to the urine treatment subsystem with the electrodeless photocatalysis is also sent to the microwave incineration subsystem.

The odor in the solid-liquid separation box 20 is sent to the electrodeless photocatalytic treatment waste gas treatment subsystem for decomposing the odor through the first odor outlet 31, the second odor outlet pipe 98, the first odor pipeline tee 155, the third odor delivery pipe 99, the second odor pipeline tee 156 and the fourth odor delivery pipe 100 through the axial flow fan 102 of the electrodeless photocatalytic treatment waste gas treatment subsystem;

in a multi-toilet system, considering the unbalanced use of toilet seats, in order to reduce the equipment volume and reasonably utilize resources, the volume of the solid-liquid separation box 20 is optimized, so that when the solid-liquid separation box 20 receives the feces which are successively emptied by the feces collection boxes 9 of a plurality of toilet seats (such as three toilet seats in a six-toilet system), the large amount of the black water is reserved because more black water is left and the electrodeless photocatalytic treatment urine treatment subsystem is not in time to treat the feces, and the waste liquid overflow port 29 is arranged to temporarily discharge the black water into the waste liquid box 124 for temporary storage through the port and the waste liquid overflow pipe 111;

the microwave incineration subsystem comprises: the sewage pump with reamer 40, the coarse pulp box 49, the electric crusher 54, the fine pulp box 56, the first self-priming pump 61, the fine pulp preheating box 63, the first stop valve 83, the second self-priming pump 85, the incineration electric valve 89 and the microwave incinerator 71; wherein:

A. the coarse pulp box 49 is provided with a coarse pulp receiving port 48, a second coarse pulp conveying pipe 53, a second full liquid level sensor 51, a first low liquid level sensor 52, a second odor outlet 50 and a first coarse pulp conveying pipe 46;

the sewage pump 40 with the reamer reams solid matters and sediments sent by the solid-liquid separation subsystem, and sends the solid matters and sediments into the coarse pulp box 49 through the first coarse pulp conveying pipe 46, when certain coarse pulp exists in the coarse pulp box 49, the first low liquid level sensor 52 acts, and the coarse pulp flows into the electric crusher 54 through the second coarse pulp conveying pipe 53 and starts to work;

the odor generated in the coarse slurry box 49 is sent to the electrodeless photocatalytic waste gas treatment subsystem for decomposing the odor through a second odor outlet 50, a first odor delivery pipe 94, an odor tee 154, a second odor delivery pipe 97, a first odor pipeline tee 155, a third odor delivery pipe 99, a second odor pipeline tee 156, a fourth odor delivery pipe 100 and an axial flow fan 102 of the electrodeless photocatalytic waste gas treatment subsystem;

the second full liquid level sensor 51 of the coarse slurry tank 49 is mainly used for alarming that the coarse slurry tank 49 is full;

B. the receiving port of the electric crusher 54 is directly communicated with the coarse pulp box 49 through the second coarse pulp conveying pipe 53 to receive the coarse pulp flowing into the coarse pulp box 49, after the electric crusher is started, the coarse pulp is further crushed and ground and is conveyed into the fine pulp box 56 through the first fine pulp conveying pipe 55 for transfer;

C. the fine pulp tank 56 is provided with a first fine pulp delivery pipe 55, a first fine pulp output port 59, a third full liquid level sensor 57, a second low liquid level sensor 58 and a first fine pulp output pipe 60;

the fine pulp crushed and ground by the electric crusher 54 directly falls into the fine pulp tank 56 by gravity, and flows into the first self-priming pump 61 through the first fine pulp output port 59 and the first fine pulp output pipe 60;

when the fine pulp tank 56 is filled with fine pulp, the third full liquid level sensor 57 acts, the first self-sucking pump 61 is started to pump the fine pulp into the fine pulp preheating tank 63, the fine pulp in the fine pulp tank 56 is gradually reduced after the first self-sucking pump 61 works, when the level of the fine pulp is low to touch the second low liquid level sensor 58 to act, the first self-sucking pump 61 stops working, and the fine pulp in the fine pulp tank 56 is completely transferred to the fine pulp preheating tank 63;

a third full liquid level sensor 57 of the fine pulp tank 56 is mainly used for alarming when the fine pulp tank 56 is full and for starting control of the first self-priming pump 61;

D. the fine pulp preheating box 63 is provided with a fine pulp inlet 67, a flue 76, a flue opening 77, a third odor outlet 96, a second fine pulp outlet 75, a flue gas inlet pipe 70, a fourth full liquid level sensor 64, a semi-liquid level sensor 65, a third low liquid level sensor 66, an annular heater 69, a temperature control sensor 68, a second fine pulp conveying pipe 62, a first odor discharging pipe 95, a flue gas discharging pipe 107, a second fine pulp output pipe 82, a first stop valve 83, a third fine pulp conveying pipe 84, a second self-priming pump 85, a fourth fine pulp conveying pipe 86, a second tee joint 87, a fifth fine pulp conveying pipe 88, an incineration electric valve 89 and a fine pulp input pipe 90;

the fine slurry sucked by the first self-sucking pump 61 from the fine slurry tank 56 is sent into the fine slurry preheating tank 63 through the second fine slurry conveying pipe 62 and the fine slurry inlet 67, when the level of the fine slurry is higher than that of the third low liquid level sensor 66, the third low liquid level sensor 66 acts, the annular heater 69 starts to work, and the temperature control sensor 68 is used for detecting the temperature of the fine slurry and controlling the work of the annular heater 69 through an intelligent control system;

the ring heater 69 only assists in the preheating of the fine pulp preheating tank 63; when the microwave incinerator 71 is not operated and the fine pulp is pumped from the fine pulp tank 56 to the fine pulp preheating tank 63, the annular heater 69 is mainly electrified to work to preheat the fine pulp, after the microwave incinerator 71 is operated, the high-temperature hot steam after solid matter incineration and the high-temperature waste gas after combustion simultaneously heat the fine pulp through the flue 76 in the fine pulp preheating tank 63, when the temperature of the fine pulp reaches a preset temperature, the intelligent control system sends out a stop instruction of the annular heater 69 to stop working, and then the fine pulp is completely preheated through the high-temperature hot steam after solid matter incineration and the high-temperature waste gas after combustion;

after the first self-sucking pump 61 is started, the fine pulp sucked from the fine pulp tank 56 is sent into the fine pulp preheating tank 63 through the second fine pulp conveying pipe 62 and the fine pulp inlet 67, when the level of the fine pulp is higher than the half liquid level sensor 65 and the fine pulp reaches a preset temperature, the second self-sucking pump 85 is started, and the preheated fine pulp is sent to the atomizing nozzle input port 74 of the microwave incinerator 71 through the second fine pulp output port 75, the second fine pulp output pipe 82, the first stop valve 83, the third fine pulp conveying pipe 84, the second self-sucking pump 85, the fourth fine pulp conveying pipe 86, the second tee 87, the fifth fine pulp conveying pipe 88, the incinerating electric valve 89 and the fine pulp input pipe 90;

after the microwave incinerator 71 works, high-temperature hot steam generated after solid matter incineration treatment and high-temperature waste gas after combustion preheat fine slurry through a flue 76 in a fine slurry preheating box 63, the high-temperature hot steam exhausted by the urine treatment subsystem after passing through a flue port 77, a flue gas exhaust pipe 107 and an electrodeless photocatalytic treatment is mixed through a third tee 108, and then the mixture is conveyed to a heat exchanger 147 through a high-temperature gas conveying pipe 109 to preheat black water conveyed to the electrodeless photocatalytic treatment urine treatment subsystem;

E. the microwave incinerator 71 is provided with an atomizing nozzle input port 74, a first compressed air input port 73, an ash residue discharge port 72 and a flue gas inlet pipe 70;

after being pressurized by a second self-sucking pump 85, the fine pulp preheated by the fine pulp preheating box 63 is sent to an atomizing nozzle of a microwave incinerator 71, atomization and drying treatment are carried out in the microwave incinerator 71, incineration is carried out in an incineration area, incinerated ash residues are temporarily stored above an ash residue discharge port 72, and cleaning and discharging treatment are carried out when the ash residues are discharged in a conditioned manner;

the air-water control device 177 feeds fresh air with certain pressure into the microwave incinerator 71 through the compressed air conveying pipe 78, the first tee joint 79, the microwave incinerator air inlet pipe 80 and the first compressed air inlet 73, so that on one hand, the fresh air is used for supporting combustion, and on the other hand, solid matters dried in a drying area of the microwave incinerator can be stirred to be fully combusted; in addition, the compressed air can blow high-temperature hot steam generated in the microwave incinerator 71 and high-temperature waste gas after combustion into the fine pulp preheating box 63 through the flue gas inlet pipe 70 to preheat fine pulp;

the system for processing the urine by the electrodeless photocatalysis comprises: electrodeless photocatalysis handles urine processing apparatus 132, high temperature supernatant input pipe 119, compressed air input pipe 81, waste liquid discharge pipe 120, high temperature steam discharge port 133, wherein be equipped with on the electrodeless photocatalysis handles urine processing apparatus 132: an atomizing nozzle 135, a supernatant inlet 134, a second compressed air inlet 137, a waste liquid outlet 136, and a high-temperature steam outlet 133;

in order to ensure the normal operation of the system, as an auxiliary system, a set of residual liquid storage device is additionally arranged in the electrodeless photocatalytic treatment urine processing subsystem, and comprises a residual liquid containing tank 124, a solid-liquid separation subsystem overflow liquid discharge port 127, an electrodeless photocatalytic treatment urine processing subsystem unprocessed supernatant liquid discharge port 128, a system cleaning effluent liquid discharge port 129, a residual liquid tank cleaning effluent discharge port 131, a residual liquid output port 126, a first residual liquid conveying pipe 121, a second electric booster pump 122, a cleaning effluent conveying pipe 91, a flushing effluent liquid electric valve 92, a discharge pipe 196, a second stop valve 197, a fifth full liquid level sensor 125 and a fourth low liquid level sensor 130;

when the feces evacuation valve 18 is closed for a certain time, the electrodeless photocatalytic treatment urine treatment device is started to preheat, a supernatant pipe in the solid-liquid separation device is conveyed to the electromagnetic valve 115 to be opened, the first electric booster pump 117 of the heat exchange subsystem works, and the pressurized supernatant with a certain pressure is conveyed to the atomizing nozzle 135 of the electrodeless photocatalytic treatment urine treatment device through the supernatant input pipe 118, the heat exchanger 147 and the supernatant input port 134 to be subjected to microwave electrodeless photocatalytic degradation sterilization treatment;

during the degradation treatment process of the supernatant, a large amount of high-temperature steam (containing a certain amount of odor, the same below) is generated, the steam sends the pressure air sent by the air source system and the high-temperature flue gas generated by the microwave incineration system into the heat exchange system to heat the supernatant input system, and the conveying paths of the high-temperature steam are as follows in sequence: a urine treatment device 132 for electrodeless photocatalytic treatment, a high-temperature steam outlet 133, a third tee 108, a high-temperature gas delivery pipe 109 and a heat exchanger 147;

the air-water control device 177 sends fresh air with certain pressure to the urine treatment device 132 through the compressed air delivery pipe 78, the first tee joint 79, the compressed air input pipe 81 and the second compressed air input port 137, so that on one hand, atomized liquid sprayed out of the atomizing nozzle 135 of the urine treatment device 132 can be stirred to be fully degraded, on the other hand, degraded high-temperature water vapor is promoted to be discharged, and circulation of the water vapor is facilitated;

because the supernatant is not fully preheated in the starting process of the urine treatment device 132 with the electrodeless photocatalytic treatment and the microwave incineration system, part of atomized water still falls to the liquid collecting area at the lower part of the urine treatment device 132 with the electrodeless photocatalytic treatment in the form of the supernatant, and is sent back to the residual liquid tank 124 through the waste liquid discharge port 136 and the waste liquid discharge pipe 120 of the urine treatment device 132 with the electrodeless photocatalytic treatment, and finally returns to the supernatant cavity of the solid-liquid separation system;

the raffinate tank 124 collects and stores:

A. the supernatant fluid overflowed by the solid-liquid separation system has the following path: the solid-liquid separation tank 20, the sewage overflow outlet 29, the sewage overflow pipe 111 and the overflow liquid discharge inlet 127 of the solid-liquid separation subsystem are discharged into the residual liquid tank 124 for temporary storage;

B. part of atomized water of the urine treatment device 132 for electrodeless photocatalytic treatment falls in the form of supernatant to a lower liquid collecting area of the urine treatment device 132 for electrodeless photocatalytic treatment, and is sent back to the residual liquid tank 124 through a waste liquid outlet 136, a waste liquid discharge pipe 120 and an untreated supernatant discharge inlet 128 of the urine treatment device 132 for electrodeless photocatalytic treatment;

C. returning system washing water: the sewage generated in the system flushing process is discharged through the fine slurry preheating box and then is sent to the residual liquid box 124 through the second fine slurry output port 75, the second fine slurry output pipe 82, the first stop valve 83, the third fine slurry conveying pipe 84, the second self-sucking pump 85, the fourth fine slurry conveying pipe 86, the second tee 87, the cleaning sewage conveying pipe 91 (the incineration electric valve 89 is closed when the flushing program is executed), the flushing sewage electric valve 92, the flushing sewage conveying pipe 93 and the system cleaning sewage discharge port 129.

The dirty liquid stored in the residual liquid tank 124 is sent to the liquid chamber of the solid-liquid separation device 20 by the second electric booster pump 122, and the conveying path is:

a residual liquid tank 124, a residual liquid outlet 126, a first residual liquid delivery pipe 121, a second electric booster pump 122, a dirty liquid return pipe 123, and a dirty liquid return inlet 30 which return to the liquid chamber of the solid-liquid separation device 20; the start of the second electric booster pump 122 is controlled by the fifth full liquid level sensor 125, when the second electric booster pump 122 is started, the raffinate is pumped to reduce the liquid level of the raffinate tank 124, and when the fourth low liquid level sensor 130 acts, the second electric booster pump 122 stops working;

if the raffinate tank 124 needs to be cleaned or the whole system needs to be stopped, the dirty liquid in the raffinate tank 124 can be completely drained, and the flow is as follows:

when the second stop valve 197 is opened, the dirty liquid in the residual liquid tank 124 is discharged through the residual liquid tank cleaning sewage outlet 131, the second stop valve 197, the second residual liquid delivery pipe 198, the four-way valve 146, the fifth drain pipe 193 and the drain joint 194; the drain joint 194 is a fire hose joint dedicated to the fire protection system, and may be connected to a nearby sewage sewer well through a fire hose to directly drain the cleaning sewage into the municipal sewage pipeline.

The electrodeless photocatalytic treatment exhaust gas treatment subsystem comprises: an electrodeless photocatalytic treatment waste gas treatment device 105, an axial flow fan 102, a waste gas input pipe 103, a waste gas input port 104 and a clean gas discharge port 106;

the odor of the solid-liquid separation subsystem and the microwave incineration subsystem and the high-temperature steam and the smoke which are generated by the heat-exchanged electrodeless photocatalytic treatment urine treatment subsystem and are not completely liquefied are sent to an electrodeless photocatalytic treatment waste gas treatment device 105 through an axial flow fan 102, a waste gas input pipe 103 and a waste gas input port 104, are subjected to the odor removal and degradation treatment of organic gas through photochemical reaction and then are discharged from a clean gas discharge port 106;

the heat exchange sub-system comprising: a heat exchanger 147, a high-temperature flue gas inlet 149, a flue gas outlet 148, a supernatant inlet 150, a high-temperature supernatant outlet 151, a second reclaimed water outlet 152, a high-temperature gas delivery pipe 109, a flue gas output pipe 101, a supernatant input pipe 118, a high-temperature supernatant input pipe 119, a first reclaimed water output pipe 153 and a first electric booster pump 117;

after the microwave incinerator 71 works, high-temperature hot steam generated after solid material incineration and high-temperature waste gas after combustion preheat fine slurry through a flue 76 in a fine slurry preheating box 63, are mixed with a high-temperature hot steam output pipe 110 discharged by an electrodeless photocatalytic treatment urine treatment subsystem through a flue port 77 and a flue gas discharge pipe 107 through a third tee 108, are sent to a heat exchanger 147 through a high-temperature gas conveying pipe 109 and a high-temperature flue gas inlet 149 to carry out heat exchange on black water sent to the electrodeless photocatalytic treatment urine treatment subsystem, are mixed with odor through a flue gas outlet 148, a flue gas output pipe 101 and a second odor pipeline tee 156, are sent to the electrodeless photocatalytic treatment waste gas treatment subsystem through an axial flow fan 102 to carry out odor removal and degradation treatment on organic gas, and are discharged from a clean gas discharge port 106;

when the fecal sewage emptying valve 18 is closed for a certain time, the electrodeless photocatalytic treatment urine treatment device is started for preheating, a supernatant pipe in the solid-liquid separation device is opened by a delivery electromagnetic valve 115, a first electric booster pump 117 of the heat exchange subsystem works to pressurize the supernatant, and then the supernatant is delivered into a heat exchanger 147 for heat exchange and temperature rise after being delivered into the atomization nozzle 135 of the electrodeless photocatalytic treatment urine treatment device through a high-temperature supernatant input pipe 119 and a supernatant input port 134, and then microwave electrodeless photocatalytic degradation sterilization treatment is carried out, wherein the supernatant is delivered into the solid-liquid separation box 20, a supernatant outlet 28, a supernatant outlet pipe 112, a supernatant stop valve 113, a supernatant pipe 114, a supernatant delivery electromagnetic valve 115, a supernatant delivery pipe 116, a first electric booster pump 117 and a supernatant input pipe 118;

high-temperature hot steam generated by the microwave incinerator, high-temperature waste gas after combustion and high-temperature hot steam discharged by the electrodeless photocatalytic treatment urine treatment subsystem exchange heat with normal-temperature supernatant liquid output by the solid-liquid separation box 20 in the heat exchanger 147, moisture in the high-temperature hot steam is condensed and separated out, and generated reclaimed water falls into a hopper-shaped reclaimed water storage area at the lower part of the heat exchanger and then falls into a reclaimed water tank 138 through a first reclaimed water output pipe 153 to be stored for preparing for reclaimed water reuse;

the flue gas after heat exchange in the heat exchanger 147 is sent to the electrodeless photocatalytic waste gas treatment subsystem for odor decomposition treatment through the heat exchanger flue gas outlet 148, the flue gas output pipe 101, the second odor pipeline tee 156 and the fourth odor delivery pipe 100 via the axial flow fan 102 of the electrodeless photocatalytic waste gas treatment subsystem.

The recycled water recycling toilet flushing subsystem comprises: well water tank 138, clear water tank 157, wherein:

A. the reclaimed water tank 138 is provided with: the reclaimed water inlet 139, the first reclaimed water outlet 142, the first overflow port 140, the first drain port 145, the sixth full liquid level sensor 141, the fifth low liquid level sensor 143, the reclaimed water pump 166, the second reclaimed water output pipe 167, the third drain pipe 189, the second drain cock 190, the first overflow pipe 144, the four-way joint 146, the fifth drain pipe 193 and the drain joint 194;

when the reclaimed water is collected to a certain degree, the sixth full liquid level sensor 141 on the reclaimed water tank 138 acts, the reclaimed water pump 166 starts to work, and the reclaimed water in the reclaimed water tank 138 is pumped into the clean water tank 157 through the first reclaimed water outlet 142, the second reclaimed water outlet pipe 167, the reclaimed water pump 166 and the reclaimed water inlet pipe 165 for flushing the toilet; when the water level of the reclaimed water in the reclaimed water tank 138 is reduced to the action of the fifth low liquid level sensor 143 or the water level in the clean water tank 157 is increased to trigger the seventh full liquid level sensor 158 of the clean water tank 157, the reclaimed water pump 166 stops working;

when the system is first used or is reused after a period of inactivity, the clear water tank 157 needs to be first filled with clear water from the ground water source;

when the middle water tank 138 is filled with the middle water, the excess middle water is discharged through the first overflow port 140, the first overflow pipe 144, the four-way 146, the fifth drain pipe 193, and the drain joint 194. The drainage joint 194 adopts a fire-fighting pipe joint special for a fire-fighting system, and can be connected to a nearby sewage drainage well through a fire-fighting pipe to directly drain cleaning sewage into an urban sewage pipeline;

before the system is deactivated, the reclaimed water in the reclaimed water tank 138 can be drained through the drainage joint 194 through the second drainage cock 190; the drainage path is as follows: the middle water tank 138, the first drain port 145, the third drain pipe 189, the second drain cock 190, the fourth drain pipe 191, the drain tee 192, the sixth drain pipe 195, the four-way 146, the fifth drain pipe 193 and the drain joint 194;

B. the clear water tank 157 is provided with: a reclaimed water inlet 161, a clean water inlet 162, a water outlet 159, a second overflow gap 199, a second water outlet 169, a seventh full liquid level sensor 158, a sixth low liquid level sensor 160, a clean water pipe 163, a clean water joint 164, a reclaimed water inlet pipe 165, a first water discharge pipe 186, a first water discharge cock 187, a fourth tee 201 and a water pipe 168;

when the system is first used or is reused after a period of inactivity, the clear water tank 157 needs to be first filled with clear water from the ground water source; the water filling path is as follows: a clean water joint 164, a clean water inlet 162 and a clean water tank 157; the clean water joint 164 adopts a fire-fighting pipe joint special for a fire-fighting system and can directly introduce clean water through a fire-fighting pipeline interface;

when the reclaimed water is collected to a certain degree, the sixth full liquid level sensor 141 on the reclaimed water tank 138 acts, the reclaimed water pump 166 starts to work, and the reclaimed water in the reclaimed water tank 138 is pumped into the clean water tank 157 through the first reclaimed water outlet 142, the second reclaimed water outlet pipe 167, the reclaimed water pump 166 and the reclaimed water inlet pipe 165 for flushing the toilet;

when a person uses the toilet, the flushing button 173 is pressed, the excrement collecting subsystem enables a flushing electromagnetic valve in the air-water control device 177 to be powered on and opened under the control of the intelligent electric control device 172 of the intelligent control subsystem and the air-water control device 177 of the air source subsystem, compressed air enters the flushing valve through one path of the flushing electromagnetic valve to enable the flushing valve to be opened, the other path of the compressed air enters the water pressurizer through the quick exhaust valve to pressurize flushing water, and pressurized pressure water enters the bedpan 1 through the flushing valve to flush the bedpan 1; after the flushing action is finished, the flushing electromagnetic valve is closed when power is lost, and the flushing valve is closed; the path of the flush water (reclaimed water or clear water) is: the clear water tank 157, the water outlet 159 and the water pipe 168 enter the air-water control device 177;

when the clean water tank 157 is filled with the reclaimed water/clean water, the redundant water is discharged through the second overflow port 199, the second overflow pipe 200, the fourth tee 201, the second drain pipe 188, the drain tee 192, the sixth drain pipe 195, the four-way 146, the fifth drain pipe 193 and the drain joint 194;

when the system is deactivated, water in the clean water tank 157 can be drained through the drain fitting 194 by the first drain cock 187; the drainage path is as follows: the clean water tank 157, the second water outlet 169, the first water outlet 186, the first water outlet cock 187, the seventh water outlet 202, the fourth tee 201, the second water outlet 188, the water outlet tee 192, the sixth water outlet 195, the four-way 146, the fifth water outlet 193 and the water outlet joint 194;

the wind source subsystem comprises: an air source 170, an air-water control device 177; wherein:

A. the air source 170 consists of a motor and a compressor, and compressed air of 10bar can be provided through a total air pipe 171;

B. the air-water control device 177 is an air-water control center of the whole system, mainly comprises an electromagnetic valve, a pressure regulating valve, a vacuum generator and a water pressurizer, can properly pressurize cleaning water for flushing the bedpan 1, vacuumizes the sewage collection box 9 through the vacuum generator, adds proper positive pressure to the sewage collection box 9, and supplies compressed air with proper pressure to the microwave incinerator 71 and the electrodeless photocatalytic treatment urine treatment device 132, and is a key system for cleaning and sewage treatment of the whole system;

the intelligent control subsystem comprises: intelligent electronic control 172, electric wire 174, liquid crystal display 175, peripheral control devices such as flush button 173, inter-use speaker, inter-use display (advertising screen), communication cable 176, sensor, switch, contactor, relay;

the intelligent control subsystem controls gas, water and electricity of the whole system according to certain logic and time sequence, can realize the functions of advertisement, entertainment and public information broadcast, has the function of accessing the Internet of things and can realize the remote monitoring of the whole system; the intelligent control subsystem is the core of the whole system;

on the basis of the above overall description of the embodiments of the invention, the following embodiments are perfected:

example 1:

as shown in fig. 1 and 2: a bedpan flushing nozzle 2 is arranged in the bedpan 1, a bedpan flushing water supply pipe system 3 is arranged outside the bedpan 1, the bottom of the bedpan flushing water supply pipe system is a feces and sewage falling port 5, and a bedpan full liquid level switch 4 is arranged on the inner side of the bedpan; after the bedpan 1 receives human excrement, the flushing button 173 is operated, the excrement collecting subsystem opens the quick drainage valve 7 under the control of the intelligent electric control device 172 of the intelligent control subsystem and the air-water control device 177 of the wind source subsystem, excrement is quickly sucked into the sewage collecting box 9 under the action of vacuum pressure in the sewage collecting box 9, and the bedpan flushing water supply system 3 supplies water with certain pressure while the quick drainage valve 7 is opened, so that the bedpan flushing nozzle 2 sprays water to flush the bedpan 1; the duration of the rinsing process may be set to 2 seconds;

when the toilet bowl 1 is filled with feces, the toilet bowl full level switch 4 outputs a toilet bowl flushing command, and the execution process of the command is consistent with the toilet bowl flushing command sent by the flushing button 173.

Example 2:

in addition to example 1, as shown in fig. 1 and 3: the main body of the dirt collecting box 9 is cylindrical and can bear certain negative pressure and positive pressure repeatedly.

Example 3:

in addition to examples 1 and 2, as shown in fig. 1 and 4: the solid-liquid separation box 20 is divided into 3 inner cavities: solid substance cavity, liquid cavity, supernatant liquid cavity.

The self-cleaning primary filter screen component 35 and the self-cleaning secondary filter screen component 32 are both designed into special meshes and box structures so as to improve the filtering efficiency of the solid-liquid separation system:

the lower part of the slide filter plate 25 is stored with a certain amount of black water for ensuring proper fluidity of the solid matter.

Example 4:

on the basis of embodiments 1 to 3, as shown in fig. 1 and 5: the sewage pump with reamer 40 will cut up the solid and deposition from the solid-liquid separation subsystem, and send it into the coarse pulp tank 49 through the first coarse pulp delivery pipe 46, when there is some coarse pulp in the coarse pulp tank 49, the first low level sensor 52 will be activated, and the coarse pulp will flow into the electric crusher 54 through the second coarse pulp delivery pipe 53 and start to work.

Example 5:

on the basis of embodiments 1 to 4, as shown in fig. 1 and 6: the fine pulp crushed and ground by the electric crusher 54 directly falls into the fine pulp tank 56 by gravity, and flows into the first self-priming pump 61 through the first fine pulp output port 59 and the first fine pulp output pipe 60.

Example 6:

in addition to embodiments 1 to 5, as shown in fig. 1 and 7: the fine pulp sucked from the fine pulp tank 56 by the first self-priming pump 61 is sent into the fine pulp preheating tank 63 through the second fine pulp conveying pipe 62 and the fine pulp inlet 67, and the temperature control sensor 68 is used for detecting the temperature of the fine pulp and controlling the work of the annular heater 69 through an intelligent control system.

Example 7:

based on embodiments 1 to 6, as shown in fig. 1 and 8: the fine slurry preheated by the fine slurry preheating box 63 is pressurized by the second self-sucking pump 85 and then sent to the atomizing nozzle of the microwave incinerator 71 to be atomized and dried in the microwave incinerator and incinerated in the incineration area, and the incinerated ash residues are temporarily stored above the ash residue discharge port 72 and cleaned and discharged when the ash residues are discharged in a condition.

The air-water control device 177 feeds fresh air with certain pressure into the microwave incinerator 71 through the compressed air delivery pipe 78, the first tee joint 79, the microwave incinerator air inlet pipe 80 and the first compressed air inlet 73, so that on one hand, the fresh air is used for supporting combustion, and on the other hand, solid matters dried in a drying area of the microwave incinerator can be stirred to be fully combusted. The compressed air blows high-temperature hot steam generated in the microwave incinerator 71 and high-temperature exhaust gas after combustion into the slurry preheating tank 63 through the flue gas inlet pipe 70 to preheat the slurry.

Example 8:

in addition to embodiments 1 to 3, as shown in fig. 1 and 9: when the feces evacuation valve 18 is closed for a certain time, the electrodeless photocatalytic treatment urine treatment device is started to preheat, the electromagnetic valve 115 for conveying the supernatant liquid pipe in the solid-liquid separation device is opened, the first electric booster pump 117 of the heat exchange subsystem works, and the pressurized supernatant liquid with a certain pressure is conveyed to the atomizing nozzle 135 of the electrodeless photocatalytic treatment urine treatment device through the heat exchanger 147, the high-temperature supernatant liquid input pipe 119 and the supernatant liquid input port 134 to be subjected to microwave electrodeless photocatalytic degradation sterilization treatment.

During the degradation treatment process of the supernatant, a large amount of high-temperature steam (containing a certain amount of odor, the same below) is generated, the steam sends the pressure air sent by the air source system and the high-temperature flue gas generated by the microwave incineration system into the heat exchange system to heat the supernatant input system, and the conveying paths of the high-temperature steam are as follows in sequence: the electrodeless photocatalytic treatment urine processing device 132, the high-temperature steam outlet 133, the third tee 108, the high-temperature gas conveying pipe 109 and the heat exchanger 147.

The air-water control device 177 sends fresh air with certain pressure to the urine treatment device 132 through the compressed air delivery pipe 78, the first tee joint 79, the compressed air input pipe 81 and the second compressed air input port 137, so that on one hand, liquid sprayed out from an atomizing nozzle of the urine treatment device 132 subjected to the electrodeless photocatalytic treatment can be stirred to be fully degraded, on the other hand, the degraded high-temperature water vapor is promoted to be discharged, and the circulation of the water vapor is facilitated.

Because the supernatant is not fully preheated in the starting process of the urine treatment device by the electrodeless photocatalytic treatment and the microwave incineration system, part of atomized water still falls to a liquid collecting area at the lower part of the urine treatment device by the electrodeless photocatalytic treatment in the form of the supernatant, and is sent back to the residual liquid tank 124 through the waste liquid discharge port 136 and the waste liquid discharge pipe 120 of the urine treatment device 132 by the electrodeless photocatalytic treatment and finally returns to a supernatant cavity of the solid-liquid separation system.

Example 9:

in addition to embodiments 1 to 3 and 8, as shown in fig. 1 and 10: the raffinate tank 120 collects and stores:

the supernatant fluid overflowed by the solid-liquid separation system has the following path: the solid-liquid separation tank 20, the sewage overflow outlet 29, the sewage overflow pipe 111 and the overflow liquid discharge inlet 127 of the solid-liquid separation subsystem are discharged into the residual liquid tank 120 for temporary storage.

Part of atomized water of the urine treatment device for electrodeless photocatalytic treatment falls to a liquid collecting area at the lower part of the urine treatment device for electrodeless photocatalytic treatment in the form of supernatant, and is sent back to the residual liquid tank 124 through a waste liquid outlet 136, a waste liquid discharge pipe 120 and an untreated supernatant discharge inlet 128 of the urine treatment device for electrodeless photocatalytic treatment 132.

Example 10:

in addition to embodiments 1 to 8, as shown in fig. 1 and 11: after the microwave incinerator 71 works, high-temperature hot steam generated after solid material incineration and high-temperature waste gas after combustion preheat fine slurry through a flue 76 in a fine slurry preheating box 63, are mixed with a high-temperature hot steam output pipe 110 discharged by an electrodeless photocatalytic treatment urine treatment subsystem through a flue port 77 and a flue gas discharge pipe 107 through a third tee 108, are sent to a heat exchanger 147 through a high-temperature flue gas input pipe 109 and a high-temperature flue gas inlet 149 to carry out heat exchange on black water sent to the electrodeless photocatalytic treatment urine treatment subsystem, are mixed with odor through a flue gas outlet 148, a flue gas output pipe 101 and a second odor pipeline tee 156, are sent to the electrodeless photocatalytic treatment waste gas treatment subsystem through an axial flow fan 102 to carry out deodorization and degradation treatment on organic gas, and are discharged from a clean gas discharge port 106.

High-temperature hot steam generated by the microwave incinerator, high-temperature waste gas after combustion and high-temperature hot steam discharged by the electrodeless photocatalytic treatment urine treatment subsystem exchange heat with normal-temperature supernatant liquid output by the solid-liquid separation box 20 in the heat exchanger 147, moisture in the high-temperature hot steam is condensed and washed out to generate reclaimed water, the reclaimed water falls into a hopper-shaped reclaimed water storage area at the lower part of the heat exchanger, and the reclaimed water falls into a reclaimed water tank 138 through a first reclaimed water output pipe 153 to be stored for preparing for reclaimed water recycling.

Example 11;

in addition to embodiments 1 to 8 and 10, as shown in fig. 1 and 12: when the reclaimed water is collected to a certain degree, the sixth full level sensor 141 on the reclaimed water tank 138 is actuated, the reclaimed water pump 166 starts to work, and the reclaimed water in the reclaimed water tank 138 is pumped into the clean water tank 157 through the first reclaimed water outlet 142, the second reclaimed water outlet pipe 167, the reclaimed water pump 166 and the reclaimed water inlet pipe 165 for flushing the toilet. When the water level of the reclaimed water in the reclaimed water tank 138 is lowered to the action of the fifth low level sensor 143 or the water level in the clear water tank 157 is raised to trigger the seventh full level sensor 158 of the clear water tank, the reclaimed water pump 166 stops working.

When the system is first applied or is to be reused after a period of inactivity, the clear water tank 157 is first filled with clear water from the surface water source.

Example 12:

in addition to embodiments 1 to 8 and 10, as shown in fig. 1 and 13: the odor of the solid-liquid separation subsystem and the microwave incineration subsystem and the high-temperature steam and the smoke which are generated by the heat-exchanged electrodeless photocatalytic treatment urine treatment subsystem and are not completely liquefied are sent to an electrodeless photocatalytic treatment waste gas treatment device 105 through an axial flow fan 102, a waste gas input pipe 103 and a waste gas input port 104, are subjected to the odor removal and degradation treatment of organic gas through photochemical reaction, and are discharged from a clean gas discharge port 106.

Example 13;

as shown in fig. 1 and 14: when the system is first applied or is to be reused after a period of inactivity, the clear water tank 157 is first filled with clear water from the surface water source. The water filling path is as follows: clean water joint 164, clean water inlet 162, clean water tank 157. The clean water joint 164 is a fire-fighting pipe joint special for a fire-fighting system, and clean water can be directly introduced through a fire-fighting pipeline interface.

Based on the above example:

the utility model provides a filth processing method of many toilet seats remove intelligent net row WC system assembly, it includes many toilet seats at least and removes intelligent net row WC system assembly, its characterized in that: the multi-toilet-seat mobile intelligent net-drainage WC system assembly comprises ten subsystems, namely a toilet seat using subsystem, a wind source subsystem, an excrement collecting subsystem, a solid-liquid separation subsystem, a microwave incineration subsystem, an electrodeless photocatalytic treatment urine processing subsystem, an electrodeless photocatalytic treatment waste gas processing subsystem, a heat exchange system, a reclaimed water recycling toilet flushing subsystem and an intelligent control subsystem, wherein the mutual electromechanical connection and position relation of the ten subsystems are clarified in the specific implementation mode in the foregoing and are not described in detail; the system comprises a toilet seat using subsystem, a wind source subsystem and a feces collecting subsystem, wherein a vacuum negative pressure solid-liquid (solid feces, urine and flushing water) collecting system is formed by the toilet seat using subsystem, the wind source subsystem and the feces collecting subsystem, the multi-toilet seat human excrement (solid liquid) is quickly and efficiently collected, the collected solid liquid is quickly fed into a solid-liquid separation subsystem through positive pressure provided by the wind source subsystem, the solid feces and the urine (containing the flushing water) are subjected to liquid-solid two-phase separation through the solid-liquid separation subsystem, the lower phase is feces heavy phase containing urine, the feces heavy phase is crushed by a high-speed paddle and then atomized and fed into a microwave incineration subsystem for drying and complete incineration, and tail gas of the microwave incineration subsystem enters a microwave photochemical reactor of the electrodeless photocatalytic treatment waste gas treatment subsystem for degradation and; the supernatant enters the urine treatment subsystem for the electrodeless photocatalytic treatment in a spraying mode, passes through the microwave photochemical reactor under the coordination of air with proper flow provided by the air source subsystem, and organic matters in the urine are degraded into tasteless low-carbon molecular compounds under the ultraviolet light catalysis action and finally mineralized into carbon dioxide and water; the water in the exhaust gas of the electrodeless photochemical reactor (liquid) is cooled, liquefied and recovered by the heat exchange system, and is sent into a reclaimed water storage tank of the reclaimed water recycling toilet flushing subsystem for recycling use in toilet flushing; the intelligent control subsystem provides functions of automatic liquid level detection, automatic emission detection, gas-water electric control, human-computer interaction interface and Internet of things access; thus, an automatic control flow type treatment line for flushing the toilet by collecting excrement, separating solid from liquid, incinerating solid, atomizing urine, degrading by photocatalytic oxidation to mineralize and recycling mineralized water is sequentially formed.

While the foregoing has shown a detailed embodiment of the invention, it will be apparent to those skilled in the art that certain changes and modifications may be made without departing from the invention; the above description and the contents mentioned in the attached drawings are only used as illustrative examples and are not to be construed as limiting the present invention, and the multi-toilet-space mobile intelligent net-drain WC system assembly and the sewage treatment method with the above technical characteristics all fall into the protection scope of the present invention.