阅读说明：本技术 一种新型煤粉锁斗顺控自动破桥装置及应用方法 (Novel coal powder lock hopper sequential control automatic bridge breaking device and application method ) 是由 张鹏 宋太浩 胜兆泉 刘红宇 于 2021-10-11 设计创作，主要内容包括：一种新型煤粉锁斗顺控自动破桥装置及应用方法是煤化工行业生产过程中煤粉“架桥”后如何有效“破桥”技术,它用于弥补常规“下压破桥”方式的单一不足,同时消除人员手动“破桥”的操作风险,其结构关系是,煤粉锁斗的下部为锁斗底锥,煤粉锁斗的中间安装有低料位检测开关；其煤粉锁斗的顶端连接有泄压管,其泄压管上分别安装有锁斗泄压切断阀、锁斗泄压调节阀；其煤粉锁斗的底端外部连接有管道充气器,其管道充气器与煤粉缓冲罐中间由锁斗放料管道连接,在锁斗放料管道上自上而下顺序连接有上切断阀、下切断阀,其煤粉缓冲罐上安装有高料位检测开关；管道充气器的一侧连接有充气管线,其充气管线上安装有管道充气器氮气切断阀。(A novel coal powder lock hopper sequential control automatic bridge breaking device and an application method are technologies of effectively breaking a bridge after coal powder is bridged in the production process of the coal chemical industry, and are used for making up the single defect of a conventional mode of pressing down to break the bridge and eliminating the operation risk of manually breaking the bridge by personnel at the same time; the top end of the pulverized coal lock hopper is connected with a pressure relief pipe, and the pressure relief pipe is respectively provided with a lock hopper pressure relief cut-off valve and a lock hopper pressure relief regulating valve; the external part of the bottom end of the coal powder lock hopper is connected with a pipeline aerator, the middle of the pipeline aerator and the coal powder buffer tank is connected by a lock hopper discharging pipeline, an upper cut-off valve and a lower cut-off valve are sequentially connected on the lock hopper discharging pipeline from top to bottom, and a high material level detection switch is arranged on the coal powder buffer tank; one side of the pipeline aerator is connected with an aeration pipeline, and a nitrogen shut-off valve of the pipeline aerator is arranged on the aeration pipeline.)

1. A novel coal powder lock hopper sequential control automatic bridge breaking device comprises a coal powder lock hopper (1), a pressurizing flute pipe (2) in the lock hopper, a lock hopper bottom cone (3), a pipeline aerator (4), a coal powder buffer tank (5), a nitrogen stop valve (6), a nitrogen flow regulating valve (7), a bottom cone nitrogen stop valve (8), a nitrogen stop valve (9), a balance pipeline (10), an upper cut-off valve (11), a lower cut-off valve (12), a lock hopper pressure relief cut-off valve (13), a lock hopper pressure relief regulating valve (14), a lock hopper discharging upper cut-off valve (15), a lock hopper discharging lower cut-off valve (16), a low material level detection switch (17), a high material level detection switch (18), a coal powder buffer pipe and lock hopper pressure difference measuring instrument (19) and a flute pipe nitrogen flow meter (20), and is characterized in that the lower part of the coal powder lock hopper (1) is the lock hopper bottom cone (3), the middle of the coal powder lock hopper (1) is provided with the low material level detection switch (17), and the top end of the coal powder lock hopper (1) is connected with the flute pipe nitrogen flow meter (20) The pressure relief pipe is connected with a lock bucket pressure relief cut-off valve (13) and a lock bucket pressure relief regulating valve (14) which are respectively arranged on the pressure relief pipe; the external part of the bottom end of a coal powder lock hopper (1) is connected with a pipeline aerator (4), the middle of the pipeline aerator (4) and a coal powder buffer tank (5) is connected by a lock hopper discharging pipeline, an upper cut-off valve (15) and a lower cut-off valve (16) are sequentially connected on the lock hopper discharging pipeline from top to bottom, and a high material level detection switch (18) is arranged on the coal powder buffer tank (5); one side of the pipeline aerator (4) is connected with an aeration pipeline, and a pipeline aerator nitrogen shut-off valve (9) is arranged on the aeration pipeline.

2. The novel pulverized coal lock-bucket sequential control automatic bridge breaking device as claimed in claim 1, which is characterized in that: the upper part of the lock hopper bottom cone (3) is provided with a lock hopper internal filling flute pipe (2); a nitrogen charging pipeline is connected to a charging flute pipe (2) in the lock hopper, a nitrogen stop valve (6) and a nitrogen flow regulating valve (7) are sequentially connected to the nitrogen charging pipeline, and a flute pipe nitrogen flowmeter (20) is arranged between the nitrogen stop valve (6) and the nitrogen flow regulating valve (7); a bottom cone nitrogen stop valve (8) is arranged between the nitrogen pressurizing pipeline and the lock hopper bottom cone (3).

3. The novel pulverized coal lock-bucket sequential control automatic bridge breaking device as claimed in claim 1, which is characterized in that: the top end of the coal dust lock hopper (1) is connected with the middle of the coal dust buffer tank (5) through a balance pipeline (10), and an upper cut-off valve (11) and a lower cut-off valve (12) are sequentially arranged in the middle of the balance pipeline (10) from top to bottom; the upper and lower balance pipelines (10) externally connected with the upper and lower cut-off valves are connected with a pipeline, and a pulverized coal buffer tube and a lock bucket differential pressure measuring instrument (19) are arranged on the pipeline.

4. The application method of the novel coal powder lock-bucket sequential control automatic bridge breaking device as claimed in claim 1 is characterized in that: when the bridging phenomenon of the pulverized coal bucket locking equipment during blanking is judged, the sequence control program skips to execute an upper top bridge breaking program first, and a lower pressure bridge breaking program is selected and executed according to the bridge breaking effect; after the bridge breaking program is executed, whether the bridge breaking is successful or not is judged, if the bridge breaking is successful, the normal blanking program is directly returned, and the subsequent bridge breaking program is not executed; if the operation of one-time 'bridge breaking' is unsuccessful, the bridge breaking differential pressure is automatically increased by 50kpa on the basis of the original setting, and the 'top-up bridge breaking' is carried out for the second time; the program is set with the maximum execution times of 'top-up bridge breaking', and the 'bridge breaking' can not be successful after reaching the upper limit, then an alarm is sent to be converted into manual operation, and the judgment of an operator is converted into execution of 'bottom-up bridge breaking' program or manual operation; according to the load capacity of the device and the design parameters of the equipment, the frequency high-limit protection of 'top-lifting bridge-breaking' and the 'bridge-breaking pressure difference' are set, the program is set with the initial frequency of 'top-lifting bridge-breaking' and the initial 'bridge-breaking pressure difference', and the process can modify the set values of the frequency of 'top-lifting bridge-breaking' and the 'bridge-breaking pressure difference' according to the running condition.

5. The application method of the novel coal powder lock-bucket sequential control automatic bridge breaking device as claimed in claim 1 is characterized in that: the pulverized coal lock hopper (1) is timed out in normal blanking or can trigger an 'upper top bridge breaking' button by setting an operator, and an 'upper top bridge breaking' automatic program is started; the automatic program design of the 'top-up bridge breaking' is specifically entered by a normal lock hopper blanking program: the method comprises the following steps that 1, when the blanking timing of a normal coal powder lock hopper (1) is over and a lock hopper low material level detection switch (17) is not monitored, the process of top-up bridge breaking is automatically started; under the condition 2, the blanking timing of the normal coal powder lock hopper (1) is not timed, the lock hopper low material level detection switch (17) is not monitored, and an operator enters an upper top bridge breaking program by triggering an upper top bridge breaking button; and if the conditions 1 and 2 are satisfied arbitrarily, an automatic program of 'top-up bridge breaking' can be entered.

6. The application method of the novel coal powder lock-bucket sequential control automatic bridge breaking device as claimed in claim 1 is characterized in that: executing the program design of 'top-up bridge breaking' sequential control: firstly, closing an upper cutting valve (15) for discharging the lock hopper and an upper cutting valve (11) for balancing a pipeline by a program; secondly, after the upper cutting valve (15) for discharging the lock bucket and the upper cutting valve (11) of the balance pipeline are detected to be closed, the lock bucket pressure relief cutting valve (13) is opened by a program; after the opening of the lock bucket pressure relief cut-off valve (13) is monitored, a certain initial valve position x% of the lock bucket pressure relief regulating valve (14) is given by a program, the lock bucket pressure relief regulating valve (14) is opened and automatic operation is carried out, and the set value is a bridge-breaking pressure difference; thirdly, after the coal powder buffer tank and lock hopper pressure difference measuring instrument 19 is monitored to be larger than a set value of bridge-breaking pressure difference, a lock hopper pressure-relief cut-off valve (13) and a lock hopper pressure-relief regulating valve (14) are closed by a program; fourthly, after the closing of the lock hopper pressure relief cut-off valve (13) is monitored, a program opens an upper cut-off valve (15) for discharging the lock hopper and an upper cut-off valve (11) for balancing a pipeline, and starts a 'lower pressure bridge breaking blanking timer'; step five, condition 1: if the condition that the lock hopper low material level detection switch (17) is triggered is monitored, a bridge breaking procedure is skipped, wherein the bridge breaking procedure represents that the bridge breaking is successful; condition 2: if the bridge breaking blanking timing is finished, the bridge breaking count is less than 2, and meanwhile, a lock hopper low material level detection switch (17) is not triggered, the bridge breaking count is increased by 1, the bridge breaking differential pressure is increased by 50kpa, and after a lower-pressure bridge breaking blanking timer is reset, the bridge breaking is carried out again in the first step; condition 3: if the bridge breaking blanking timing is finished, the bridge breaking count is not less than or equal to 2, and the lock hopper low material level detection switch (17) is not triggered, an alarm is sent, and the bridge breaking at the top can be continuously executed or the bridge breaking is converted into the bridge breaking at the lower pressure after the manual processing of an operator.

7. The application method of the novel coal powder lock-bucket sequential control automatic bridge breaking device as claimed in claim 1 is characterized in that: a given lock hopper pressure relief regulating valve (14) has a certain initial valve position x%, and can be modified according to the valve characteristics and the size of the lock hopper; bridge breaking pressure difference = bridge breaking primary pressure difference + (bridge breaking times and pressure difference increasing value); the initial pressure difference (default 100 kpa) and the pressure difference increase value (default 50 kpa) of the broken bridge can be modified by process personnel, and the upper limit protection limitation is carried out on the broken bridge pressure difference according to the equipment safety; the upper limit of the times of executing the automatic bridge breaking can be modified, but the program execution period and the material level of downstream equipment need to be considered; after jumping out of the upper top bridge breaking sequence control, the pressure relief bridge breaking blanking timer needs to be reset, and the bridge breaking counting counter is reset to be 0.

Technical Field

The invention relates to a technology for effectively breaking a bridge after coal powder is bridged in the production process of the coal chemical industry, in particular to a novel coal powder lock hopper sequential control automatic bridge breaking device and an application method.

Background

In the process and equipment of pulverized coal in chemical and power generation industries, a lock hopper device is commonly used when the pulverized coal, ash, slag and other solid materials need to be conveyed in a variable pressure manner. Under the influence of material granularity, humidity and detention time, the lock hopper blanking process often generates a bridge bridging phenomenon, and the conventional automatic bridge breaking program design concept is to break the bridge by pressurizing the lock hopper bottom cone, the flute pipe and the pipeline aerator and by means of pressure difference pressure-down conveying. The conventional mode usually needs to be successful through multiple times of bridge breaking, time is delayed, nitrogen is wasted, particularly for the bridge bridging condition between a pipeline aerator and a blanking valve, the conventional bridge breaking mode can cause further compaction of solid materials, and the effect is poor. After the conventional automatic bridge breaking method is invalid, an operator is inevitably required to manually break the bridge, so that the burden of the operator is increased, and certain operation risk is brought. And the problem of bridging of the lock hopper can be effectively solved by finding the mode of 'pushing up and breaking the bridge' of the pressure relief airflow of the lock hopper during manual 'bridge breaking'. At present, the automatic 'bridge breaking' process sequence control concept of the lock hopper equipment still stays in the traditional lock hopper pressurization 'bridge breaking' mode.

Disclosure of Invention

The invention aims to provide a novel safe and efficient coal powder lock hopper sequential control automatic bridge breaking device and an application method thereof, which are used for overcoming the single defect of the conventional 'bridge breaking by pressing down', meanwhile, the invention eliminates the operational risk of manual bridge breaking of personnel, and the invention aims to realize the operation of the coal powder bridge breaker, which comprises a coal powder lock hopper, a pressure-charging flute pipe in the lock hopper, a lock hopper bottom cone, a pipeline aerator, a coal powder buffer tank, a cut-off valve, a nitrogen flow regulating valve, a bottom cone nitrogen cut-off valve, a balance pipeline, an upper cut-off valve, a lower cut-off valve, a lock hopper pressure-discharging cut-off valve, a lock hopper discharging upper cut-off valve, a lock hopper discharging lower cut-off valve, a low material level detection switch, a high material level detection switch, a coal powder and lock hopper differential pressure measurement instrument, and a flute pipe nitrogen buffer pipe, the lower part of the coal powder lock hopper is a lock hopper bottom cone, and the middle of the coal powder lock hopper is provided with a low material level detection switch; the top end of the pulverized coal lock hopper is connected with a pressure relief pipe, and the pressure relief pipe is respectively provided with a lock hopper pressure relief cut-off valve and a lock hopper pressure relief regulating valve; the external part of the bottom end of the coal powder lock hopper is connected with a pipeline aerator, the middle of the pipeline aerator and the coal powder buffer tank is connected by a lock hopper discharging pipeline, an upper cut-off valve and a lower cut-off valve are sequentially connected on the lock hopper discharging pipeline from top to bottom, and a high material level detection switch is arranged on the coal powder buffer tank; one side of the pipeline aerator is connected with an aeration pipeline, and a nitrogen shut-off valve of the pipeline aerator is arranged on the aeration pipeline.

The upper part of the lock hopper bottom cone is provided with a lock hopper internal filling flute pipe; a nitrogen inflation pipeline is connected to a pressurization flute pipe in the lock hopper, a nitrogen stop valve and a nitrogen flow regulating valve are sequentially connected to the nitrogen inflation pipeline, and a flute pipe nitrogen flowmeter is arranged between the nitrogen stop valve and the nitrogen flow regulating valve; a bottom cone nitrogen cut-off valve is arranged between the nitrogen inflation pipeline and the lock hopper bottom cone.

The top end of the coal powder lock hopper is connected with the middle of the coal powder buffer tank through a balance pipeline, and an upper cut-off valve and a lower cut-off valve are sequentially arranged in the middle of the balance pipeline from top to bottom; the upper and lower balance pipelines externally connected with the upper and lower cut-off valves are connected with a pipeline, and a pulverized coal buffer tube and a lock bucket differential pressure measuring instrument are arranged on the pipeline.

The device is used for manually starting the 'top-up bridge-breaking' program by an operator and can be provided with a 'top-up bridge-breaking' button. The button can be set as an external electronic mechanical button or a built-in HMI panel soft button.

The application method of the invention comprises the following steps: when the bridging phenomenon of the pulverized coal bucket locking equipment during blanking is judged, the sequence control program skips to preferentially execute a top-pushing bridge-breaking program, and a bottom-pressing bridge-breaking program is selected according to the bridge-breaking effect; after the bridge breaking program is executed, whether bridge breaking is successful or not is judged by detecting a lock hopper low material level detection switch, if yes, the normal blanking program is directly returned, and a subsequent bridge breaking program is not executed; if the operation of one-time 'bridge breaking' is unsuccessful, the bridge breaking differential pressure is automatically increased by 50kpa on the basis of the original setting, and the 'top-up bridge breaking' is carried out for the second time; the program is set with the maximum execution times of 'top-up bridge breaking', and the 'bridge breaking' can not be successful after reaching the upper limit, then an alarm is sent to be converted into manual operation, and the judgment of an operator is converted into execution of 'bottom-up bridge breaking' program or manual operation; according to the load capacity of the device and the design parameters of the equipment, the frequency high-limit protection of 'top-lifting bridge-breaking' and the 'bridge-breaking pressure difference' are set, the program is set with the initial frequency of 'top-lifting bridge-breaking' and the initial 'bridge-breaking pressure difference', and the process can modify the set values of the frequency of 'top-lifting bridge-breaking' and the 'bridge-breaking pressure difference' according to the running condition.

The normal blanking timing of the coal powder lock hopper is overtime or the automatic program start of the top-loading bridge-breaking can be triggered by manually triggering a top-loading bridge-breaking button by an operator; specifically, the normal lock hopper blanking program enters the automatic program design of 'top-up bridge breaking': the method comprises the following steps that 1, if the normal lock hopper blanking timing is reached and a lock hopper low material level detection switch is not monitored, an 'top-up bridge breaking' program is automatically started; and 2, under the condition that the normal coal powder lock hopper is not fed for a while, and the lock hopper low material level detection switch is not monitored, an operator enters an upper top bridge breaking program by triggering an upper top bridge breaking button. And if the conditions 1 and 2 are satisfied arbitrarily, an automatic program of 'top-up bridge breaking' can be entered.

Executing the program design of 'top-up bridge breaking' sequential control: firstly, closing an upper cutting valve for discharging the lock hopper and an upper cutting valve for balancing a pipeline by a program; secondly, after the upper cutting valve of the discharging of the lock hopper and the upper cutting valve of the balance pipeline are detected to be closed, the program opens the pressure relief cut-off valve of the lock hopper; after the situation that the lock bucket pressure relief cut-off valve is opened is monitored, a certain initial valve position x% of the lock bucket pressure relief regulating valve is set by a program, the lock bucket pressure relief regulating valve is opened and put into operation automatically, and the set value is a broken bridge pressure difference; thirdly, after the coal powder buffer tank and lock hopper pressure difference measuring instrument 19 is monitored to be larger than a set value of bridge-breaking pressure difference, closing the lock hopper pressure-relief cut-off valve and the lock hopper pressure-relief regulating valve by a program; fourthly, after the closing of the lock hopper pressure relief cut-off valve is monitored, the program opens the upper cut-off valve of the lock hopper discharging and the upper cut-off valve of the balance pipeline, and starts a 'lower pressure bridge breaking discharging timer'; step five, condition 1: if the condition that the lock hopper low material level detection switch is triggered is monitored, a bridge breaking procedure is carried out, wherein the bridge breaking procedure represents that the bridge breaking is successful; condition 2: if the bridge breaking blanking timing is finished, the bridge breaking count is less than 2, and meanwhile, a lock hopper low material level detection switch is not triggered, the bridge breaking count is increased by 1, the bridge breaking differential pressure is increased by 50kpa, and after the bridge pressing blanking timer is reset, the bridge breaking is carried out again in the first step; condition 3: if the bridge breaking blanking timing is finished, the bridge breaking count is not less than or equal to 2, and the lock hopper low material level detection switch is not triggered, an alarm is sent, and after manual processing by an operator, the bridge breaking by pushing up can be continuously executed or the bridge breaking by pressing down can be continuously executed.

A given lock hopper pressure relief regulating valve has a certain initial valve position x%, and can be modified according to the valve characteristics and the size of the lock hopper; bridge breaking pressure difference = bridge breaking primary pressure difference + (bridge breaking times and pressure difference increasing value); the initial pressure difference (default 100 kpa) and the pressure difference increase value (default 50 kpa) of the broken bridge can be modified by process personnel, and the upper limit protection limitation is carried out on the broken bridge pressure difference according to the equipment safety; the upper limit of the times of executing the automatic bridge breaking can be modified, but the program execution period and the material level of downstream equipment need to be considered; after jumping out of the upper top bridge breaking sequence control, the pressure relief bridge breaking blanking timer needs to be reset, and the bridge breaking counting counter is reset to be 0.

The significance of the invention is as follows: 1. the defect that a conventional bridge breaking mode is single is overcome, and a lock hopper pressure relief type bridge breaking process is added; 2. the bottleneck problem that the conventional bridge breaking mode can aggravate material compaction and is not suitable for successful bridge breaking when the bridge is built between the bottom of the lock hopper and the blanking valve is solved; 3. the pressure relief type bridge breaking operation method forms an automatic sequential control bridge breaking procedure, so that the operation is convenient and fast; 4. the operation risk of manually relieving pressure to break the bridge by operators is eliminated; 5. the 'bridge breaking' method is suitable for coal powder locking hoppers and other solid material locking hoppers with similar conditions; 6. it can be directly applied to the design of new devices and the technical transformation of old devices; 7. no equipment investment is required to be increased; 8. the design of changeable 'bridge breaking' times and 'bridge breaking' pressure difference can pertinently solve the problem of different coal powder 'bridge building' severity, so that an operator can determine the next 'bridge breaking' degree according to the 'bridge breaking' effect last time, the treatment time is shortened to the maximum degree, and nitrogen is saved, therefore, the method is a solution without investment and with quick effect.

Drawings

Fig. 1 is a schematic structural diagram of a novel sequential control automatic bridge breaker of a pulverized coal lock bucket, wherein 1 is a pulverized coal lock bucket 2, a pressure filling flute pipe 3 in the lock bucket, a lock bucket bottom cone 4, a pipeline aerator 5, a pulverized coal buffer tank 6, a nitrogen shut-off valve 7, a nitrogen flow regulating valve 8, a bottom cone nitrogen shut-off valve 9, a pipeline aerator nitrogen shut-off valve 10, a balance pipeline 11, an upper cut-off valve 12, a lower cut-off valve 13, a lock bucket pressure relief shut-off valve 14, a lock bucket pressure relief regulating valve 15, a lock bucket discharging upper cut-off valve 16, a lock bucket discharging lower cut-off valve 17, a lock bucket low material level detection switch 18, a high material level detection switch 19, a pulverized coal buffer pipe and lock bucket differential pressure measurement instrument 20 and a flute pipe nitrogen flow meter.

Detailed Description

The device comprises a coal powder lock hopper 1, a pressure-charging flute pipe 2 in the lock hopper, a lock hopper bottom cone 3, a pipeline aerator 4, a coal powder buffer tank 5, a nitrogen stop valve 6, a nitrogen flow regulating valve 7, a bottom cone nitrogen stop valve 8, a nitrogen stop valve 9, a balance pipeline 10, an upper cut-off valve 11, a lower cut-off valve 12, a lock hopper pressure-discharging cut-off valve 13, a lock hopper pressure-discharging regulating valve 14, a lock hopper discharging upper cut-off valve 15, a lock hopper discharging lower cut-off valve 16, a low material level detection switch 17, a high material level detection switch 18, a coal powder buffer pipe and lock hopper differential pressure measurement instrument 19 and a flute pipe nitrogen flowmeter 20, wherein the lower part of the coal powder lock hopper 1 is the lock hopper bottom cone 3, and the middle of the coal powder lock hopper 1 is provided with the low material level detection switch 17; the top end of a coal powder lock hopper 1 is connected with a pressure relief pipe, and a lock hopper pressure relief cut-off valve 13 and a lock hopper pressure relief regulating valve 14 are respectively arranged on the pressure relief pipe; the external part of the bottom end of a coal powder lock hopper 1 is connected with a pipeline aerator 4, the middle of the pipeline aerator 4 and a coal powder buffer tank 5 is connected by a lock hopper discharging pipeline, an upper cut-off valve 15 and a lower cut-off valve 16 are sequentially connected on the lock hopper discharging pipeline from top to bottom, and a high material level detection switch 18 is arranged on the coal powder buffer tank 5; one side of the pipeline aerator 4 is connected with an aeration pipeline, and a pipeline aerator nitrogen shut-off valve 9 is installed on the aeration pipeline.

In the embodiment 2, the upper part of the lock hopper bottom cone 3 is provided with a lock hopper internal pressurizing flute pipe 2; a nitrogen charging pipeline is connected to a charging flute pipe 2 in the lock hopper, a nitrogen cut-off valve 6 and a nitrogen flow regulating valve 7 are sequentially connected to the nitrogen charging pipeline, and a flute pipe nitrogen flowmeter 20 is arranged between the nitrogen cut-off valve 6 and the nitrogen flow regulating valve 7; a bottom cone nitrogen cut-off valve 8 is arranged between the nitrogen pressurizing pipeline and the lock hopper bottom cone 3.

In embodiment 3, the top end of the pulverized coal lock hopper 1 is connected with the middle of the pulverized coal buffer tank 5 through a balance pipeline 10, and an upper cut-off valve 11 and a lower cut-off valve 12 are sequentially arranged in the middle of the balance pipeline 10 from top to bottom; the upper and lower balance pipelines 10 externally connected with the upper and lower cut-off valves are connected with a pipeline, and a pulverized coal buffer tube and a lock bucket differential pressure measuring instrument 19 are arranged on the pipeline.

Example 4, application method of the invention: when the bridging phenomenon of the pulverized coal bucket locking equipment during blanking is judged, the sequence control program skips to execute an upper top bridge breaking program first, and a lower pressure bridge breaking program is selected and executed according to the bridge breaking effect; after the bridge breaking program is executed, whether the bridge breaking is successful or not is judged, if the bridge breaking is successful, the normal blanking program is directly returned, and the subsequent bridge breaking program is not executed; if the operation of one-time 'bridge breaking' is unsuccessful, the bridge breaking differential pressure is automatically increased by 50kpa on the basis of the original setting, and the 'top-up bridge breaking' is carried out for the second time; the program is set with the maximum execution times of 'top-up bridge breaking', and the 'bridge breaking' can not be successful after reaching the upper limit, then an alarm is sent to be converted into manual operation, and the judgment of an operator is converted into execution of 'bottom-up bridge breaking' program or manual operation; according to the load capacity of the device and the design parameters of the equipment, the frequency high-limit protection of 'top-lifting bridge-breaking' and the 'bridge-breaking pressure difference' are set, the program is set with the initial frequency of 'top-lifting bridge-breaking' and the initial 'bridge-breaking pressure difference', and the process can modify the set values of the frequency of 'top-lifting bridge-breaking' and the 'bridge-breaking pressure difference' according to the running condition.

In the embodiment 5, the pulverized coal lock hopper 1 is overtime in normal blanking timing or can trigger an automatic program starting of top-up bridge breaking by setting an operator to trigger a top-up bridge breaking button; the automatic program design of the 'top-up bridge breaking' is specifically entered by a normal lock hopper blanking program: under the condition 1, when the blanking timing of the normal coal powder lock hopper 1 is up and the lock hopper low material level detection switch 17 is not monitored, the process of top-loading bridge breaking is automatically started; and 2, under the condition that the normal pulverized coal lock hopper 1 is not fed with the timing, the lock hopper low material level detection switch 17 is not monitored, and an operator enters an upper top bridge breaking program by triggering an upper top bridge breaking button. And if the conditions 1 and 2 are satisfied arbitrarily, an automatic program of 'top-up bridge breaking' can be entered.

Example 6, the program design of the "top-up bridge breaking" sequential control is executed: firstly, closing an upper cutting valve 15 for discharging the lock hopper and an upper cutting valve 11 for balancing a pipeline by a program; secondly, after the upper cutting valve 15 of the discharging of the lock bucket and the upper cutting valve 11 of the balance pipeline are detected to be closed, the lock bucket pressure relief cut-off valve 13 is opened by a program; after the opening of the lock bucket pressure relief cut-off valve 13 is monitored, a certain initial valve position x% of the lock bucket pressure relief regulating valve 14 is given by a program, the lock bucket pressure relief regulating valve 14 is opened and automatic, and the set value is a bridge-breaking pressure difference; thirdly, after the coal powder buffer tank and lock hopper pressure difference measuring instrument 19 is monitored to be larger than a set value of bridge breaking pressure difference, closing the lock hopper pressure relief cut-off valve 13 and the lock hopper pressure relief regulating valve 14 by a program; fourthly, after the closing of the lock hopper pressure relief cut-off valve 13 is monitored, the program opens the lock hopper discharging upper cut-off valve 15 and the upper cut-off valve 11 for balancing the pipeline, and starts a 'lower pressure bridge breaking discharging timer'; step five, condition 1: if the condition that the lock hopper low material level detection switch 17 is triggered is monitored, a bridge breaking procedure is carried out, wherein the bridge breaking procedure represents that the bridge breaking is successful; condition 2: if the bridge breaking blanking timing is finished, the bridge breaking count is less than 2, and the lock hopper low material level detection switch 17 is not triggered, the bridge breaking count is increased by 1, the bridge breaking differential pressure is increased by 50kpa, and after the bridge pressing blanking timer is reset, the bridge breaking is carried out again in the first step; condition 3: if the bridge breaking blanking timing is finished, the bridge breaking count is not less than or equal to 2, and the lock hopper low material level detection switch 17 is not triggered, an alarm is sent, and the bridge breaking at the top can be continuously executed or the bridge breaking is converted into the bridge breaking at the lower pressure after the manual processing of an operator.

Example 7, a given lock hopper pressure relief regulating valve 14 has a certain initial valve position x%, which can be modified according to the valve characteristics and the size of the lock hopper; bridge breaking pressure difference = bridge breaking primary pressure difference + (bridge breaking times and pressure difference increasing value); the initial pressure difference (default 100 kpa) and the pressure difference increase value (default 50 kpa) of the broken bridge can be modified by process personnel, and the upper limit protection limitation is carried out on the broken bridge pressure difference according to the equipment safety; the upper limit of the times of executing the automatic bridge breaking can be modified, but the program execution period and the material level of downstream equipment need to be considered; after jumping out of the upper top bridge breaking sequence control, the pressure relief bridge breaking blanking timer needs to be reset, and the bridge breaking counting counter is reset to be 0.