阅读说明：本技术 一种三塔制氧系统 (Three-tower oxygen generation system ) 是由 赵锐 金浩 于 2019-10-22 设计创作，主要内容包括：本发明公开了一种三塔制氧系统,包括空气压缩机、后冷却器、冷干机和三个分子筛塔,空气压缩机上设有过滤器；每个分子筛塔上均设有进气端、排气端和出氧端,分子筛塔的进气端设有第一阀门,分子筛塔的排气端设有第二阀门,冷干机通过第一阀门和三个分子筛塔的进气端分别相连；任意两分子筛塔之间连通,任意两连通的分子筛塔之间设有第三阀门,每个分子筛塔的出氧端连有氧气缓冲罐,氧气缓冲罐连有氧气储气罐；氧气缓冲罐和氧气储气罐之间还设有第一氧控仪和两位三通阀,两位三通阀的进气端与第一氧控仪相连,两位三通阀的一个出气端与氧气储气罐相连,两位三通阀的另一个出气端为不合格氧气排放端。本发明应用于制氧技术领域。(The invention discloses a three-tower oxygen generation system, which comprises an air compressor, an after cooler, a cold dryer and three molecular sieve towers, wherein the air compressor is provided with a filter; each molecular sieve tower is provided with an air inlet end, an air outlet end and an oxygen outlet end, the air inlet end of each molecular sieve tower is provided with a first valve, the air outlet end of each molecular sieve tower is provided with a second valve, and the freeze-drying machine is respectively connected with the air inlet ends of the three molecular sieve towers through the first valves; any two molecular sieve towers are communicated, a third valve is arranged between any two communicated molecular sieve towers, the oxygen outlet end of each molecular sieve tower is connected with an oxygen buffer tank, and the oxygen buffer tank is connected with an oxygen storage tank; still be equipped with first oxygen between oxygen buffer tank and the oxygen gas holder and control appearance and two three-way valves, the inlet end of two three-way valves links to each other with first oxygen and control the appearance, and one of two three-way valves is given vent to anger and is held with the oxygen gas holder and link to each other, and another of two three-way valves is given vent to anger and is held for unqualified oxygen emission. The invention is applied to the technical field of oxygen generation.)

1. The three-tower oxygen generation system is characterized by comprising an air compressor, an after cooler, a cold dryer and three molecular sieve towers, wherein the air compressor, the after cooler and the cold dryer are sequentially connected, and a filter is arranged on the air compressor;

each molecular sieve tower is provided with an air inlet end, an air outlet end and an oxygen outlet end, the air inlet end of each molecular sieve tower is provided with a first valve, the air outlet end of each molecular sieve tower is provided with a second valve, and the cold dryer is respectively connected with the air inlet ends of the three molecular sieve towers through the first valves;

any two molecular sieve towers are communicated, a third valve is arranged between any two communicated molecular sieve towers, the oxygen outlet end of each molecular sieve tower is connected with an oxygen buffer tank, and the oxygen buffer tank is connected with an oxygen storage tank;

still be equipped with first oxygen accuse appearance and two three-way valves between oxygen buffer tank and the oxygen gas holder, the inlet end of two three-way valves links to each other with first oxygen accuse appearance, one of two three-way valves gives vent to anger the end and links to each other with the oxygen gas holder, another of two three-way valves gives vent to anger the end and is unqualified oxygen emission end.

2. The three-tower oxygen generation system according to claim 1, wherein a first one-way valve is arranged between the molecular sieve tower and the oxygen buffer tank, an overflow valve is arranged between the oxygen buffer tank and the oxygen storage tank, and a pressure sensor is arranged on the oxygen storage tank.

3. The three-tower oxygen generation system of claim 1, further comprising a box, wherein the air compressor, the aftercooler, the freeze dryer, the molecular sieve tower, the oxygen buffer tank and the oxygen storage tank are all arranged in the box, the box is provided with an air vent and an exhaust fan, and an air duct is formed between the air vent and the exhaust fan.

4. The three tower oxygen generation system of claim 3, wherein a damper spring is disposed between the air compressor and the tank.

5. The three tower oxygen generation system of claim 3, wherein filter cotton is disposed on the vent.

6. The three tower oxygen generation system of claim 3, wherein sound deadening cotton is affixed to the interior of the tank.

7. The three-tower oxygen generation system as claimed in claim 1, wherein the outlet end of the oxygen storage tank is connected with an oxygen sterilization filter and a second oxygen control instrument in sequence.

8. The three-tower oxygen generation system according to claim 7, wherein a pressure reducing valve, a throttle valve, a flow meter and a second one-way valve are sequentially connected between the oxygen sterilizing filter and the second oxygen controller.

9. The three-tower oxygen generation system as claimed in claim 1, wherein the gas outlet end of each second valve is connected to a main exhaust pipe, and an exhaust muffler is arranged on the main exhaust pipe.

10. The three-tower oxygen generation system of claim 1, wherein a fine dust filter is connected between the freeze dryer and each molecular sieve tower.

Technical Field

The invention belongs to the technical field of oxygen generation, and particularly relates to a three-tower oxygen generation system.

Background

At present, a common oxygen generator is a double-adsorption-tower oxygen generator, one adsorption tower is used for absorbing air to generate oxygen, the other adsorption tower is used for resolving oxygen in a molecular sieve by using finished product oxygen to complete a cycle period, the oxygen generation efficiency is low, and the oxygen recovery rate of the process mode is about 40%; secondly, when the two adsorption towers are switched, the pressure difference is large, so that an air buffer tank needs to be configured, and the air inlet pipe generates pipeline noise when the two adsorption towers are switched; thirdly, the compressed air generally adopts a micro-oil screw compressor, oil-gas separation and gas post-cooling treatment are required, the volume is generally large, and in order to ensure the service life of the molecular sieve, the oil content in the gas needs to be removed layer by layer through a multi-stage filter; in order to deeply remove water in the compressed air, a two-stage mode of a cold dryer and a suction dryer is generally adopted, and the automatic drainage is adopted at regular time, so that the gas waste is more, and the economy is not good; therefore, the whole system has a complex structure, large volume and occupied area, high noise (generally 75-85 dB (A)), high manufacturing and production cost, and can generate qualified oxygen only after being started for 20-30 min.

The patent document with the application number of CN200920115154.X discloses a nitrogen making machine with a three-tower structure, which is provided with a tower A, a tower B and a tower C, wherein the bottom of the tower A is connected with a valve I, a valve IV and a valve VII in parallel, the bottom of the tower B is connected with a valve II, a valve V and a valve VIII in parallel, and the bottom of the tower C is connected with a valve III, a valve VI and a valve IX in parallel; the middle parts of the tower A, the tower B and the tower C are respectively externally connected with a valve ten, a valve eleven and a valve twelve; the top of the tower A is connected with a valve thirteen and a valve sixteen in parallel, the top of the tower B is connected with a valve fourteen and a valve seventeen in parallel, the top of the tower C is connected with a valve fifteen and a valve eighteen in parallel, the other ends of the valve thirteen, the valve fourteen and the valve fifteen are connected with a pipe five-way, and the other ends of the valve sixteen, the valve seventeen and the valve eighteen are connected with a; the tops of the tower A, the tower B and the tower C are respectively communicated with a one-way valve I, a one-way valve II and a one-way valve III, and the other ends of the one-way valve I, the one-way valve II and the one-way valve III are communicated with a pipe VII; the second pipe is provided with an air inlet, and the third pipe and the fourth pipe bypass each other.

The above patent documents disclose the principle of three-tower oxygen production, but air entering the adsorption tower is not treated at all, which seriously affects the quality of oxygen production, and the quality of oxygen supplied on the oxygen pipeline manufactured by the adsorption tower cannot be guaranteed.

Disclosure of Invention

The invention mainly aims to provide a three-tower oxygen generation system which is high in oxygen generation efficiency, does not generate large noise and can ensure the quality of the generated oxygen.

In order to achieve the purpose, the invention provides a three-tower oxygen generation system, which comprises an air compressor, an after cooler, a cold dryer and three molecular sieve towers, wherein the air compressor, the after cooler and the cold dryer are sequentially connected, and the air compressor is provided with a filter;

each molecular sieve tower is provided with an air inlet end, an air outlet end and an oxygen outlet end, the air inlet end of each molecular sieve tower is provided with a first valve, the air outlet end of each molecular sieve tower is provided with a second valve, and the cold dryer is respectively connected with the air inlet ends of the three molecular sieve towers through the first valves;

any two molecular sieve towers are communicated, a third valve is arranged between any two communicated molecular sieve towers, the oxygen outlet end of each molecular sieve tower is connected with an oxygen buffer tank, and the oxygen buffer tank is connected with an oxygen storage tank;

still be equipped with first oxygen accuse appearance and two three-way valves between oxygen buffer tank and the oxygen gas holder, the inlet end of two three-way valves links to each other with first oxygen accuse appearance, one of two three-way valves gives vent to anger the end and links to each other with the oxygen gas holder, another of two three-way valves gives vent to anger the end and is unqualified oxygen emission end.

In a further improvement, a one-way valve is arranged between the molecular sieve tower and the oxygen buffer tank, an overflow valve is arranged between the oxygen buffer tank and the oxygen gas storage tank, and a pressure sensor is arranged on the oxygen gas storage tank.

Further improved, a three tower system oxygen system still includes the box, air compressor, aftercooler, cold machine, molecular sieve tower, oxygen buffer tank, oxygen gas holder are all established in the box, be equipped with air vent and exhaust fan on the box, form the wind channel between air vent and the exhaust fan.

In a further improvement, a damping spring is arranged between the air compressor and the box body.

In a further improvement, the vent holes are provided with filter cotton.

In a further improvement, the box body is internally pasted with silencing cotton.

In a further improvement, the air outlet end of the oxygen storage tank is sequentially connected with an oxygen sterilization filter and a second oxygen control instrument.

In a further improvement, a pressure reducing valve, a throttle valve, a flow meter and a one-way valve are sequentially connected between the oxygen sterilization filter and the second oxygen controller.

In a further improvement, the air outlet end of each second valve is respectively connected to a main exhaust pipe, and an exhaust silencer is arranged on the main exhaust pipe.

In a further improvement, a precise dust removal filter is connected between the cold dryer and each molecular sieve tower.

Compared with the prior art, the technical scheme of the invention has the beneficial effects that:

when the air-cooled air dryer is used for producing oxygen, air enters the air compressor through the filter, the air compressor compresses the air, the compressed air is cooled by the aftercooler, then water is removed from the cooling dryer, the water removal effect can be ensured after the water is removed after the water is cooled, and the water can be removed deeply. The air after deep dehydration enters the molecular sieve towers through the first valves respectively, the three molecular sieve towers alternately generate oxygen, the oxygen generated by the molecular sieve is buffered in the oxygen buffer tank, and finally the oxygen is stored in the oxygen storage tank.

The first oxygen control instrument is arranged between the oxygen buffer tank and the oxygen storage tank and used for detecting the quality of oxygen, when the detected oxygen quality is unqualified, the oxygen is discharged through an unqualified oxygen discharge end of the two-position three-way valve, and when the oxygen detection is qualified, the oxygen of the oxygen buffer tank is introduced into the oxygen storage tank through the two-position three-way valve to be stored.

The air is treated before oxygen generation, so that the moisture in the air is removed; oxygen is detected after oxygen generation, unqualified oxygen is discharged, and the quality of the prepared oxygen is ensured.

The recovery rate of oxygen production is 45-50%, and the pressure swing adsorption efficiency is improved compared with that of a double-tower pressure swing adsorption system. When the oxygen generating device is used for generating oxygen, the pressure difference is small and stable when the two molecular sieve towers are switched, no extra pipeline noise is generated, and an air buffer tank does not need to be configured.

The air compressor can adopt an oil-free compressor, oil removal measures are not needed due to the adoption of the oil-free compressor, an air buffer tank is not needed, the molecular sieve contains a deep water removal molecular sieve, an additional suction dryer is not needed for water removal, a large amount of space and structure are saved, the occupied area can be reduced, and integrated assembly is realized. The invention can generate qualified oxygen within 10min after starting up.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the structures shown in the drawings without creative efforts.

FIG. 1 is a schematic flow diagram of a three column oxygen generation system;

FIG. 2 is a schematic diagram of a three-column oxygen generation system;

FIG. 3 is another schematic diagram of a three column oxygen generation system.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.

It should be noted that all the directional indicators (such as up, down, left, right, front, and rear … …) in the embodiment of the present invention are only used to explain the relative position relationship between the components, the movement situation, etc. in a specific posture (as shown in the drawing), and if the specific posture is changed, the directional indicator is changed accordingly.

In addition, the descriptions related to "first", "second", etc. in the present invention are only for descriptive purposes and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one such feature. In the description of the present invention, "a plurality" means at least two or more, for example, three or the like, unless specifically defined otherwise.

In the present invention, unless otherwise expressly stated or limited, the terms "connected," "secured," and the like are to be construed broadly, and for example, "secured" may be a fixed connection, a removable connection, or an integral part; can be mechanically or electrically connected; they may be directly connected or indirectly connected through intervening media, or they may be connected internally or in any other suitable relationship, unless expressly stated otherwise. The specific meanings of the above terms in the present invention can be understood by those skilled in the art according to specific situations.

In addition, the technical solutions in the embodiments of the present invention may be combined with each other, but it must be based on the realization of those skilled in the art, and when the technical solutions are contradictory or cannot be realized, such a combination of technical solutions should not be considered to exist, and is not within the protection scope of the present invention.

As shown in fig. 1 to 3, a three-tower oxygen generation system comprises an air compressor 1, an after cooler 2, a cold dryer 3 and three molecular sieve towers 4, wherein the air compressor 1, the after cooler 2 and the cold dryer 3 are connected in sequence, and a filter 11 is arranged on the air compressor 1; the air compressor 1 adopts an oil-free compressor, does not need an oil-gas separator and a multi-stage filter to remove oil, and saves a large amount of space and structure. Be equipped with the automatic rejector of electron liquid level 31 on the cold machine of doing 3, can the automatic drainage through the automatic rejector of electron liquid level 31, it discharges in real time according to the actual output of condensate, and intelligence and almost no air loss. On the other hand, the molecular sieve tower 4 contains the deep water absorption molecular sieve, and the water absorption molecular sieve is regenerated without extra waste gas, so that the oxygen generation efficiency of the three-tower oxygen generation system is high.

Each molecular sieve tower 4 is provided with an air inlet end, an air outlet end and an oxygen outlet end, the air inlet end of each molecular sieve tower 4 is provided with a first valve 41, the air outlet end of each molecular sieve tower 4 is provided with a second valve 42, and the cold dryer 3 is respectively connected with the air inlet ends of the three molecular sieve towers 4 through the first valves 41;

any two molecular sieve towers 4 are communicated, a third valve 43 is arranged between any two communicated molecular sieve towers 4, the oxygen outlet end of each molecular sieve tower 4 is connected with an oxygen buffer tank 5, and the oxygen buffer tank 5 is connected with an oxygen storage tank 6;

still be equipped with first oxygen accuse appearance 51 and two three-way valve 52 between oxygen buffer tank 5 and the oxygen gas holder 6, the inlet end of two three-way valve 52 links to each other with first oxygen accuse appearance 51, and one of two three-way valve 52 is given vent to anger and is held and link to each other with oxygen gas holder 6, and another of two three-way valve 52 is given vent to anger and is held 521 for unqualified oxygen discharge end.

First valve 41, second valve 42, third valve 43 are the solenoid valve, and the solenoid valve is the normal close formula, and after three tower system oxygen system shut down, the internal pressure of oxygen buffer tank 5, molecular sieve tower 4 all can not reduce, consequently can get back to the state when shutting down automatically when three tower system oxygen system restart, reaches the target oxygen concentration in the 10min of start.

The oxygen generation principle of the three molecular sieve towers 4 is as follows:

the molecular sieve tower 4 is divided into a tower A, a tower B and a tower C; taking tower A as an example, the method specifically comprises the following steps: 1. adsorption: when the tower A is pressurized and then continuously enters air, the air is adsorbed under certain pressure, and before a concentration penetration point at the oxygen outlet end of the tower A does not appear, namely a section of unused adsorbent layer is still remained at the tail end of the tower top of the tower A, the tower A can still adsorb certain nitrogen. At the moment, part of the oxygen prepared by the tower A enters an oxygen buffer tank 5, and the other part of the oxygen enters the tower B and is used for boosting the pressure of the tower B; 2. primary pressure equalizing drop: continuously connecting the tower A with the tower B, stopping air inflow of the tower A, and starting air inflow of the tower B until the pressures of the two towers are balanced, thereby completing the step of uniform pressure drop; 3. secondary pressure equalizing drop: the tower A is connected with the tower C, and oxygen produced by the tower A provides cleaning gas for the tower C; 4. emptying: opening a second valve 42 at the exhaust end of the tower A to reduce the pressure of the tower A to the minimum and remove a part of the nitrogen adsorbed in the tower A; 5. cleaning: the tower A is connected with the tower B, part of oxygen prepared by the tower B is used for cleaning the tower A, and residual nitrogen in the tower A is cleaned to regenerate the tower A; 6. pressure equalization and rise: closing a second valve 42 at the exhaust end of the tower A, connecting the tower A with the tower C, and using part of oxygen prepared by the tower C for boosting the pressure of the tower A; 7. boosting pressure: and continuously connecting the tower A with the tower C, stopping air inlet of the tower C, starting air inlet of the tower A until the pressure of the two towers is balanced, finishing the step of boosting, and repeating the steps by the tower A.

The steps performed by the towers A, B and C are the same, and the towers A, B and C alternately perform the steps in sequence. When the tower A is used for generating oxygen, the tower A is used for boosting the pressure of the tower B, and the tower A is used for cleaning the tower C at the same time; correspondingly, when the tower B is used for preparing oxygen, the pressure of the tower C is increased at the same time, and the tower A is cleaned; when the tower C produces oxygen, the pressure of the tower A is increased, and the tower B is cleaned at the same time. Thus, the alternating oxygen generation of the tower A, the tower B and the tower C is realized, and the continuous oxygen generation can be ensured.

In this embodiment, a first check valve 44 is arranged between the molecular sieve tower 4 and the oxygen buffer tank 5, an overflow valve 53 is arranged between the oxygen buffer tank 5 and the oxygen storage tank 6, and a pressure sensor 61 is arranged on the oxygen storage tank 6. The pressure sensor 61 can detect the pressure inside the oxygen gas tank 6, that is, the oxygen content inside the oxygen gas tank 6. The oxygen storage tank 6 may be formed in a plurality of parallel oxygen storage tank groups. The pressure that overflow valve 53 set for is the minimum adsorption pressure in molecular sieve tower 4, and oxygen buffer tank 5 and first check valve 44 cooperate and provide the absorption backpressure for molecular sieve tower 4, like this, only when adsorption pressure surpassed the pressure in oxygen buffer tank 5, the oxygen end just had oxygen to go out of molecular sieve tower 4 passes through first check valve 44 and gets into in oxygen buffer tank 5, and then steps such as step up, wash with being slightly less than oxygen buffer tank 5 pressure in other molecular sieve towers 4.

In this embodiment, a three tower system oxygen system still includes box 7, air compressor 1, aftercooler 2, cold machine 3 that does, molecular sieve tower 4, oxygen buffer tank 5, oxygen gas holder 6 all establishes in box 7, other hardware structure of this embodiment all can integrate in box 7, entire system compact structure is reasonable, high integration, the volume reduces more than 50% with the product of production, area reduces more than 40%, and installation gyro wheel can conveniently remove bottom box 7, manufacturing and on-the-spot installation cost reduce. The case 7 is provided with a vent hole 71 and an exhaust fan 72, and an air passage is formed between the vent hole 71 and the exhaust fan 72. The air convection between the inside of the box body 7 and the outside can be enhanced through the vent holes 71, the exhaust fan 72 and the air channel formed by the vent holes, fresh air can enter the box body 7 quickly, and nitrogen discharged by the molecular sieve tower 4 can be discharged in time.

In this embodiment, a damper spring 73 is provided between the air compressor 1 and the case 7. The vibration of the air compressor 1 is not transmitted to the case 7 at all, and noise can be reduced.

In this embodiment, be equipped with the filter pulp on the air vent 71, the filter pulp can carry out prefiltering to the air that gets into air vent 71, improves the quality of entering air.

In this embodiment, the box 7 is inside to be pasted with the amortization cotton, also pastes the amortization cotton on the door plant of box 7, can the noise reduction.

In this embodiment, the air outlet end of the oxygen storage tank 6 is sequentially connected with an oxygen sterilization filter 62 and a second oxygen control instrument 63. Oxygen bacteria removal filter 62 can filter the oxygen bacteria removal, and second oxygen accuse appearance 63 is used for carrying out the secondary to oxygen and detects, guarantees the quality of oxygen.

In this embodiment, a pressure reducing valve 64, a throttle valve 65, a flow meter 66 and a second check valve 67 are further connected between the oxygen sterilizing filter 62 and the second oxygen controller 63 in sequence. A pressure reducing valve 64 is used to reduce the flow rate, a throttle valve 65 is used to control the flow, a flow meter 66 is used to monitor the flow size, and a second check valve 67 is used to prevent the reverse flow of oxygen.

The oxygen sterilization filter 62, the pressure reducing valve 64, the throttle valve 65, the flow meter 66, the second check valve 67 and the second oxygen control instrument 63 are all integrated inside the box body 7, and oxygen led out from the second oxygen control instrument 63 can be directly connected with a main pipe of a hospital for oxygen supply without additional field installation.

The three-tower oxygen generation system realizes automatic control through a PLC or a singlechip and displays or sets system parameters in real time through a touch screen; the control system is provided with a cloud server, data transmission is carried out by utilizing a GPRS network or an Ethernet, and the running condition of the system can be monitored in real time through a mobile phone client or a remote monitoring center; when a fault or an abnormality occurs, the alarm information can be instantly prompted in a mobile phone client, a remote monitoring center and a short message mode.

In this embodiment, the gas outlet end of each second valve 42 is integrally connected to the main exhaust pipe 8, and the exhaust muffler 81 is disposed on the main exhaust pipe 8, so as to reduce noise generated during nitrogen gas exhaust. The damping spring 73 is used for damping and silencing, the silencing cotton is used for silencing, and the exhaust silencer 81 is used for silencing, so that the noise of the whole machine is controlled within 65dB (A).

In this embodiment, there is a fine dust removal filter 9 connected between the cooling dryer 3 and each molecular sieve tower 4, and the fine dust removal filter can filter air and remove dust in the air.

The above description is only a preferred embodiment of the present invention, and is not intended to limit the scope of the present invention, and all modifications and equivalents of the present invention, which are made by the contents of the present specification and the accompanying drawings, or directly/indirectly applied to other related technical fields, are included in the scope of the present invention.