CN218565142U - Deoxynitriding device capable of preventing pipeline from being blocked - Google Patents

Abstract

The application discloses can prevent deoxidation nitrogen device that pipeline blockked up, can prevent deoxidation nitrogen device that pipeline blockked up is used for getting rid of the oxygen and/or the nitrogen gas that contain in the chemical substance such as octafluorocyclobutane that stores in at least a storage bottle, the storage bottle has a filling port. The deoxidation nitrogen device capable of preventing pipeline blockage comprises at least one flow control assembly, wherein the flow control assembly comprises a first flow measuring part and at least one first control valve, the first flow measuring part is connected with the filling port formed in the storage bottle through a pipeline so as to enable the gas mixture to flow out through the filling port, in the flowing-out process, the first flow measuring part is used for detecting the discharge flow of the gas mixture, the discharge flow of the gas mixture is detected, and when the discharge flow of the gas mixture is detected to be overlarge, the first control valve is used for regulating the discharge flow of the gas mixture.

Description

Deoxynitriding device capable of preventing pipeline from being blocked

Technical Field

The utility model relates to a deoxidation nitrogen device technical field especially relates to can prevent deoxidation nitrogen device of pipeline jam.

Background

In the production process of the chemical substances, the content of oxygen and nitrogen in the raw materials is high, so that impurities such as oxygen or nitrogen and the like may be mixed in the filled filling bottle, for example, the oxygen or nitrogen is mixed in the filled octafluorocyclobutane. Meanwhile, the air contains oxygen or nitrogen, which may further cause impurities such as oxygen or nitrogen in the filling bottle during the process of filling chemical substances. In order to improve the purity of the chemical substances in the filling bottles, it is important to effectively remove oxygen or nitrogen from the chemical substances. The chemical substance is in a liquid state at the lower part and in a gaseous state at the upper part in the steel cylinder. Oxygen and nitrogen are distributed in both the liquid and gaseous states of the chemical substance, in equilibrium. When the concentration of oxygen or nitrogen in the liquid (gas) state changes, the corresponding concentration of oxygen or nitrogen in the gas (liquid) state also changes correspondingly, so as to reach the balance.

Conventionally, when oxygen or nitrogen in chemical substances is removed, a worker usually opens a valve of a filled filling bottle directly to discharge the oxygen and nitrogen in the filling bottle along with the gaseous state of the chemical substances, and the chemical substances liquefy when encountering cold during the discharge process, which easily causes pipeline blockage and affects the discharge effect of the oxygen and nitrogen.

Simultaneously at the discharge process, oxygen and nitrogen gas in the filling bottle can't keep gathering in the top of filling bottle with high concentration all the time for the discharge efficiency of oxygen and nitrogen gas is not high.

In addition, when oxygen and nitrogen gas are discharged through the valve, the discharged gas discharge flow can not be detected, so that the discharged gas discharge flow can not be found when being large, and finally, chemical gas is easily discharged excessively, and the waste of chemical substances is caused.

SUMMERY OF THE UTILITY MODEL

The utility model has the advantages of a provide can prevent deoxidation nitrogen device that pipeline blockked up, when discharging gas mixture, the atmospheric pressure in the pipeline is in the negative pressure state when guaranteeing to discharge to reduce chemical gas's liquefaction temperature through reducing pressure, and then avoid temperature variation to lead to the gas liquefaction to cause the jam, consequently improve and detach gas mixture's effect.

The utility model discloses an advantage lies in providing the deoxidation nitrogen device that can prevent the pipeline jam, through when discharging gas mixture, monitors the flow that gas mixture discharged to the too big chemical gas who leads to storing in the storage bottle of flow discharges the excessive quantity when avoiding gas mixture to discharge, leads to discharging the most chemical gas of storing in the storage bottle together and causes the waste.

The utility model has the advantages of a provide can prevent deoxidation nitrogen device that pipeline blockked up, through setting up the effect of getting rid of oxygen and nitrogen gas in the simple structure improvement storage bottle, need not set up complicated structure and operate, and then reduce cost.

The utility model discloses an advantage lies in providing the deoxidation nitrogen device that can prevent the pipeline jam, and the storage bottle heats the gas in the storage bottle when discharging gas mixture, improves the relative volatility of nitrogen gas and/or oxygen in the storage bottle for oxygen and/or nitrogen gas volatilize from liquid more easily, and then improve the concentration of oxygen and/or nitrogen gas of the gaseous state of gathering in the storage bottle, can discharge most oxygen and/or nitrogen gas during the feasible emission.

The utility model discloses an advantage lies in providing the deoxidation nitrogen device that can prevent the pipeline jam, through when the exhaust gas mixture, utilizes the temperature difference for chemical gas can precool the liquefaction and take place the backward flow, reduces the in-process chemical gas's of exhaust gas mixture emission, improves and discharges the effect.

For reaching the utility model discloses above at least one advantage, the utility model provides a can prevent deoxidation nitrogen device of pipeline jam, deoxidation nitrogen device that can prevent pipeline jam is used for getting rid of the gas mixture of storing in the at least storage bottle, the storage bottle has one and fills the filler hole, deoxidation nitrogen device that can prevent pipeline jam includes:

the flow control assembly comprises at least one first control valve, the first control valve is arranged on a pipeline externally connected with the storage bottle and is arranged at one end, far away from the storage bottle, of the pipeline, and the flow of the gas mixture discharged through the pipeline is regulated and controlled through the first control valve;

the pressure control and pressing part is connected with the first control valve through a pipeline, the pressure control and pressing part comprises a vacuum generator, the vacuum generator is connected with the first control valve through a pipeline, and the pressure in the pipeline connected between the vacuum generator and the first control valve is adjusted to be in a negative pressure state through the vacuum generator.

According to the utility model discloses an embodiment, can prevent deoxidation nitrogen device of pipeline jam includes a first side stream piece, first side stream piece install in the storage bottle with on the pipeline that sets up between the first control valve, first side stream piece has an import and an export, the import with the storage bottle has the filling port communicates each other, and through first side stream piece detects the gas mixture is followed the storage bottle fill port exhaust flow.

According to the utility model discloses an embodiment, vacuum generator has an air inlet, a vacuum port and a gas outlet, can prevent that the deoxidation nitrogen device of pipeline jam still includes an air compression subassembly, the air compression subassembly includes an air compression piece, the air compression piece with form in vacuum generator through the pipeline intercommunication between the air inlet, through the air compression piece is with external air compression.

According to the utility model discloses an embodiment, the accuse casting die still includes a second control valve, the second control valve set up in vacuum generator with on the pipeline that sets up between the first control valve.

According to an embodiment of the utility model, the control casting die still includes a third control valve, the third control valve set up in vacuum generator is close to air inlet department, through the third control valve control opening and closing of air inlet.

According to the utility model discloses an embodiment, the accuse casting die still includes a fourth control valve, the fourth control valve set up in vacuum generator is close to gas outlet department, through the fourth control valve control opening and closing of gas outlet.

According to the utility model discloses an embodiment, the air compression subassembly still includes a fifth control valve, the fifth control valve set up in the air compression piece with on the pipeline that sets up between the vacuum generator, through the fifth control valve control the opening and closing of air compression piece.

According to the utility model discloses an embodiment, the accuse flows the subassembly and still includes a second current surveying piece, the second current surveying set up in air compression spare with set up between the vacuum generator on the pipeline, through the second current surveying piece detects the follow air compression spare lets in vacuum generator's compressed air's flow size.

According to the utility model discloses an embodiment, can prevent deoxidation nitrogen device that pipeline blockked up still includes a pressure measurement subassembly, pressure measurement subassembly includes a pressure measurement spare, the pressure measurement spare set up in first control valve with on the pipeline that sets up between the vacuum generator, through the pressure measurement spare detects first control valve with the pressure value in the pipeline that sets up between the vacuum generator.

According to the utility model discloses an embodiment, can prevent deoxidation nitrogen device of pipeline jam still includes a constant temperature spare, constant temperature spare set up in the storage bottle is and can heat up.

Drawings

Fig. 1 shows a schematic structural diagram of a deoxidation nitrogen device capable of preventing pipeline blockage according to the invention.

Fig. 2 shows a schematic structural diagram of the deoxygen device part capable of preventing pipeline blockage according to the invention.

Fig. 3 shows a schematic structural diagram of the local deoxygen device capable of preventing pipeline blockage according to the present invention.

Detailed Description

The following description is presented to disclose the invention so as to enable any person skilled in the art to practice the invention. The preferred embodiments in the following description are given by way of example only, and other obvious variations will occur to those skilled in the art. The underlying principles of the invention, as defined in the following description, may be applied to other embodiments, variations, modifications, equivalents, and other technical solutions without departing from the spirit and scope of the invention.

It will be understood by those skilled in the art that in the present disclosure, the terms "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc., indicate orientations or positional relationships that are based on those shown in the drawings, which are merely for convenience in describing the present invention and to simplify the description, and are not intended to indicate or imply that the device or element so referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus the terms are not to be construed as limiting the invention.

It is understood that the terms "a" and "an" should be interpreted as meaning "at least one" or "one or more," i.e., that a quantity of one element may be one in one embodiment, while a quantity of another element may be plural in other embodiments, and the terms "a" and "an" should not be interpreted as limiting the quantity.

Referring to fig. 1 to 3, a pipeline blockage prevention nitrogen deoxo device according to a preferred embodiment of the present invention for removing oxygen and/or nitrogen contained in a chemical substance such as octafluorocyclobutane stored in at least one storage bottle 900 is described in detail below, and the storage bottle 900 has a filling port 9001. Preferably, the storage bottle 900 is implemented as a steel bottle.

It will be understood by those skilled in the art that the chemical is stored in the storage bottle 900 in a lower liquid state and an upper gaseous state due to evaporation. When the filling port 9001 is opened, the gas state of the chemical substance is exhausted from the filling port 9001.

The density of the chemical gas is greater than that of oxygen and greater than that of nitrogen, and when the storage bottle 900 is left standing for a long time, higher-concentration oxygen and/or nitrogen can be collected above the inner cavity of the storage bottle 900. However, when oxygen and/or nitrogen gas is continuously discharged, the oxygen and/or nitrogen gas and the chemical gas cannot achieve the layering effect as if they are left standing for a long time, and the layering is not obvious. Therefore, when oxygen and/or nitrogen gas in the inner cavity of the storage bottle 900 is discharged, a part of the chemical substances stored in the storage bottle 900 is discharged together. In other words, when the oxygen and/or nitrogen gas in the storage bottle 900 is discharged, a gas mixture of the oxygen and/or nitrogen gas and the chemical substance is actually discharged.

The device for removing oxygen and nitrogen capable of preventing pipeline blockage comprises at least one flow control assembly 10, wherein the flow control assembly 10 comprises a first flow measuring part 11 and at least one first control valve 12, the first flow measuring part 11 is connected with the filling port 9001 formed in the storage bottle 900 through a pipeline so as to enable the gas mixture to flow out through the filling port 9001, in the flowing out process, the discharge flow of the gas mixture is detected through the first flow measuring part 11, so that the discharge flow of the gas mixture is detected, and when the discharge flow of the gas mixture is detected to be overlarge, the discharge flow of the gas mixture is regulated through the first control valve 12, so that the situation that the chemical substances stored in the storage bottle 900 are all discharged and waste is caused due to the overlarge discharge flow of the gas mixture is avoided.

The first flow-measuring member 11 has an inlet 1101 and an outlet 1102, the inlet 1101 and the filling port 9001 of the storage bottle 900 communicate with each other, and the first control valve 12 is installed at the outlet 1102 of the first flow-measuring member 11 to control the degree of opening of the outlet 1102. It will be appreciated by those skilled in the art that when the outlet 1102 is opened to a greater degree, the flow of the gas mixture exiting the outlet 1102 is excessive; when the outlet 1102 is opened to a small degree, the discharge flow rate of the gas mixture from the outlet 1102 becomes small, thereby achieving the purpose of adjusting the discharge flow rate of the gas mixture.

Preferably, the first flow measuring element 11 is embodied to comprise a flow meter by means of which the discharge flow of the gas mixture is detected.

Preferably, the first control valve 12 is implemented to include a flow regulating valve, with which the degree to which the outlet 1102 is opened is controlled, thus adjusting the discharge flow rate of the gas mixture. Thus, when it is desired to discharge the gas mixture from the storage bottle 900, the first control valve 12 is opened, the gas mixture flows out along the filling port 9001, and then the gas mixture is discharged in the direction from the inlet 1101 to the outlet 1102 of the first flow measuring element 11. In addition, when the gas mixture is discharged, the magnitude of the flow rate of the gas mixture discharged is detected by the first flow measuring part 11, and when the first flow measuring part 11 detects that the flow rate of the gas mixture discharged is too large, the opening degree of the outlet 1102 is controlled by the first control valve 12, so that the flow rate of the gas mixture discharged from the outlet 1102 is reduced, so that the gas mixture is slowly discharged from the outlet 1102, thereby preventing the chemical substance stored in the storage bottle 900 from being discharged at one time due to the too large flow rate of the gas mixture when the gas mixture is directly and rapidly discharged from the filling port 9001, and preventing the chemical substance stored in the storage bottle 900 from being wasted.

Further, the deoxygen device capable of preventing pipeline blockage further comprises a constant temperature part 20, wherein the constant temperature part 20 is arranged on the storage bottle 900 and can be heated to heat the storage bottle 900, the storage bottle 900 is heated and then is kept warm, the temperature of the storage bottle 900 is kept constant, the relative volatility of oxygen and/or nitrogen in the storage bottle 900 is improved, the oxygen and/or nitrogen in the storage bottle 900 is enabled to be rapidly gathered above the storage bottle 900, the concentration of the oxygen and/or nitrogen gathered above the storage bottle 900 is improved, and the proportion of the oxygen and/or nitrogen in the discharged gas mixture is further improved. In other words, the discharge amount of oxygen and/or nitrogen can be increased.

Preferably, the constant temperature member 20 is implemented to include a heater blanket wrapping the lower body of the storage bottle 900 to heat the chemical substance in a liquid phase state inside the storage bottle 900.

It should be noted that, when the lower body of the storage bottle 900 is heated by the thermostatic element 20, the temperature of the upper body of the storage bottle 900 is lower than that of the lower body. Therefore, when the chemical gas mixture is discharged from the filling port 9001, the chemical gas is not discharged from the filling port 9001, and when the chemical gas mixture passes through the upper bottle body, the chemical gas is liquefied by cooling due to the low temperature of the upper bottle body, and then the amount of the chemical gas discharged is reduced, so that the waste of the chemical gas is reduced.

It will be appreciated by those skilled in the art that the storage bottle 900 cannot be completely filled when filling the chemical into the storage bottle 900. Thus, the chemical remains in a gaseous state where the storage bottle 900 is adjacent to the filling port 9001. In other words, when filling the chemical into the storage bottle 900, the chemical near the upper side in the storage bottle 900 is in a gas phase state, and the chemical near the lower side in the storage bottle 900 is in a liquid phase state. When the gas mixture contained in the chemical substance is removed, the gas mixture near the upper portion is discharged from the filling port 9001, and the concentration ratio of the gas phase and the liquid phase in the storage bottle 900 is a certain value during the discharge, so that oxygen and/or nitrogen is continuously precipitated from the liquid phase at the bottom, thereby improving the effect of removing oxygen and/or nitrogen.

Preferably, the thermostatic element 20 is arranged to maintain the temperature of the storage bottle 900 between 30 ℃ and 50 ℃.

Further, the device for removing oxygen and nitrogen capable of preventing pipeline blockage further comprises a control and pressing element 30, and the control and pressing element 30 is connected with the first control valve 12 through a pipeline. The control member 30 includes a vacuum generator 31, the vacuum generator 31 is connected to the first control valve 12 through a pipeline, so that after the first control valve 12 is opened, the gas mixture will continue to flow through the pipeline arranged between the vacuum generator 31 and the first control valve 12, and during the flow, the vacuum generator 31 adjusts the pressure in the pipeline connected between the vacuum generator 31 and the first control valve 12 to be in a balanced and stable negative pressure state, and reduces the pressure value in the pipeline. It will be understood by those skilled in the art that the smaller the pressure value of the gas mixture, the lower the liquefaction temperature of the gas mixture, and therefore the lower the liquefaction temperature of the gas mixture by reducing the pressure value in the pipeline after the gas mixture is discharged from the pipeline in order to avoid liquefaction of the chemical gases in the gas mixture. In this way, clogging due to liquefaction of the chemical gas in the gas mixture after the gas mixture is discharged from the pipeline is avoided.

In other words, when the heated gas mixture is discharged from the outlet 1102, since the subsequent pipeline is not heated, the temperature in the pipeline is lower than that in the storage bottle 900, and thus if the gas mixture is directly discharged from the outlet 1102, the chemical gas in the gas mixture is liquefied upon cooling. By setting the pressure control member 30, the pressure value in the pipeline is reduced, so that the liquefaction temperature of the chemical gas in the gas mixture entering the pipeline is reduced, and even if the temperature in the subsequent pipeline is lower than the temperature in the storage bottle 900, the chemical gas in the gas mixture is not liquefied, thereby avoiding the blockage of the pipeline in the process of discharging the gas mixture.

Preferably, two to twenty sets of flow control assemblies 10 are provided, each set of flow control assemblies 10 is respectively mounted to each different storage bottle 900, and all flow control assemblies 10 are communicated with the control pressure member 30 through the same pipeline.

Specifically, the vacuum generator 31 has an air inlet 3101, a vacuum port 3102 and an air outlet 3103, the device for preventing nitrogen oxide from being blocked by a pipeline further comprises an air compression assembly 40, the air compression assembly 40 comprises an air compression member 41, the air compression member 41 is communicated with the air inlet 3101 of the vacuum generator 31 through a pipeline, air is compressed by the air compression member 41, the air is input into the vacuum generator 31 from the air inlet 3101, the gas mixture is guided to flow through the vacuum port 3102 by negative pressure, and finally the air is completely discharged from the air outlet 3103.

It will be understood by those skilled in the art that the atmosphere inside the pipe line disposed between the vacuum generator 31 and the first control valve 12 is in a negative pressure state, that is, the gas mixture is sucked from the vacuum port 3102 by the negative pressure through the pipe line disposed between the vacuum generator 31 and the first control valve 12, and finally the gas mixture discharged from the first control valve 12 is guided to be discharged through the gas outlet 3103 disposed on the vacuum generator 31.

Further, the control member 30 further includes a second control valve 32, and the second control valve 32 is disposed on a pipe provided between the vacuum generator 31 and the first control valve 12, so that the opening and closing of the vacuum port 3102 of the vacuum generator 31 is controlled by the second control valve 32.

Preferably, the second control valve 32 is implemented to include a solenoid valve to control the opening and closing of the vacuum port 3102 by the solenoid valve.

Further, the control member 30 further includes a third control valve 33, and the third control valve 33 is disposed near the gas inlet 3101 of the vacuum generator 31, so that the opening and closing of the gas inlet 3101 are controlled by the third control valve 33.

Preferably, the third control valve 33 is implemented to include a solenoid valve to control the opening and closing of the intake port 3101 by the solenoid valve.

Further, the control member 30 further includes a fourth control valve 34, and the fourth control valve 34 is disposed near the gas outlet 3103 of the vacuum generator 31, so as to control the opening and closing of the gas outlet 3103, and close the gas outlet 3103 after the gas-liquid mixture is completely discharged.

Preferably, the fourth control valve 34 is implemented to include a solenoid valve to control the opening and closing of the gas outlet 3103 by the solenoid valve.

Further, the air compressing assembly 40 further includes a fifth control valve 42, and the fifth control valve 42 is disposed on a pipeline disposed between the air compressing member 41 and the vacuum generator 31 to control the opening and closing of the air compressing member 41.

Preferably, the fifth control valve 42 is implemented to include a solenoid valve to control the opening and closing of the air compressing member 41 by the solenoid valve.

Further, the flow control assembly 10 further includes a second flow measuring member 13, the second flow measuring member 13 is disposed on a pipeline disposed between the air compressing member 41 and the vacuum generator 31, and the flow rate of the compressed air introduced from the air compressing member 41 into the pipeline is detected by the second flow measuring member 13.

Preferably, the second flow measuring element 13 is embodied as a flow meter.

Further, the deoxynitrogen device capable of preventing the pipeline from being blocked further comprises a pressure measuring assembly 50, the pressure measuring assembly 50 comprises a pressure measuring piece 51, the pressure measuring piece 51 is arranged on a pipeline arranged between the first control valve 12 and the vacuum generator 31, and the pressure value in the pipeline arranged between the first control valve 12 and the vacuum generator 31 is detected through the pressure measuring piece 51, so that the pressure in the pipeline can be visually detected.

In other words, the pressure value in the pipe provided between the first control valve 12 and the vacuum generator 31 is monitored by the pressure measuring member 51, so that the pressure change in the pipe provided between the first control valve 12 and the vacuum generator 31 when the gas mixture is discharged can be visually reflected, and the pressure value in the pipe provided between the first control valve 12 and the vacuum generator 31 is monitored to ensure that the pressure value is within a controllable range.

Preferably, the pressure-measuring element 51 is implemented to comprise a pressure gauge.

Further, the pressure measuring assembly 50 further includes a sixth control valve 52, and the sixth control valve 52 is installed on a pipe provided between the pressure measuring member 51 and the first control valve 12 to control the opening and closing of the pressure measuring member 51, and when pressure measurement is required, the sixth control valve 52 is opened.

Preferably, the sixth control valve 52 is implemented to include a solenoid valve.

Furthermore, can prevent deoxidation nitrogen device of pipeline jam still includes a temperature measurement piece 60, temperature measurement piece 60 install in the storage bottle 900, through temperature measurement piece 60 detects the temperature of storage bottle 900, and then it is right the temperature of storage bottle 900 heating detects to avoid the temperature of heating to hang down or too high influence the exhaust effect of gas mixture.

Further, can prevent deoxidation nitrogen device of pipeline jam still includes a temperature control piece 70, is using can prevent deoxidation nitrogen device of pipeline jam, will can prevent deoxidation nitrogen device of pipeline jam arranges a space in and uses, temperature control piece 70 is set up and can be regulated and control the temperature in the space makes storage bottle 900 uses in a stable environment to it can not be right to ensure that ambient temperature can not lead to the fact the influence storage bottle 900's temperature. In other words, when the lower body of the storage bottle 900 is heated by the thermostatic element 20, the upper body of the storage bottle 900 is prevented from being affected by the change of the external temperature, and the temperature control element 70 is arranged to ensure that a certain temperature difference exists between the lower body of the storage bottle 900 and the upper body of the storage bottle 900, so that the chemical gas can be pre-cooled and liquefied during the process of transferring the chemical gas from the lower body to the upper body, and then the chemical gas reflows, thereby improving the reflowing effect of the chemical gas.

Preferably, the temperature controlling member 70 is implemented to include an air conditioner.

The working method of the deoxidation nitrogen device capable of preventing the pipeline from being blocked mainly comprises the following steps:

when the first control valve 12 is opened, the gas mixture in the storage bottle 900 flows out from the filling port 9001, and the gas mixture flows out from the storage bottle 900 by using the second flow measuring part 13.

The working method of the nitrogen oxide removing device capable of preventing the pipeline from being blocked also comprises the following steps:

the fourth control valve 34, the third control valve 33 and the second control valve 32 are opened, and the air compression member 41 is opened, and then the first control valve 12 is opened again, so that a stable negative pressure is formed, and the gas mixture flowing out of the filling port 9001 is guided to flow out of the vacuum port 3102 by the negative pressure, and finally flows out of the vacuum port 3102 to the air outlet 3103.

The air compressor 41 discharges the compressed air from the air inlet 3101 into the vacuum generator 31, and a constant negative pressure difference is generated, thereby preventing the pressure of the storage bottle 900 from changing during the process of discharging the gas mixture.

Further, the working method of the deoxidation nitrogen device capable of preventing pipeline blockage further comprises the following steps:

the pressure measuring assembly 50 is used for detecting the pressure in the pipeline, so that the pressure value in the pipeline is ensured to be in a controllable range in the process of discharging the gas mixture, and the phenomenon that the pipeline is blocked due to the fact that the temperature in the pipeline is influenced by overlarge pressure change is avoided.

It will be understood by those skilled in the art that the embodiments of the present invention described above and shown in the drawings are given by way of example only and are not limiting of the present invention. The advantages of the present invention are already complete and effectively realized. The functional and structural principles of the present invention have been shown and described in the embodiments without departing from the principles, embodiments of the present invention may have any deformation or modification.

Claims (10)

1. Can prevent deoxidation nitrogen device that pipeline blockked up, deoxidation nitrogen device that can prevent pipeline blockked up is used for getting rid of the gas mixture of storing in at least a storage bottle, the storage bottle has a filling port, its characterized in that, deoxidation nitrogen device that can prevent pipeline blockking up includes:

the flow control assembly comprises at least one first control valve, the first control valve is arranged on a pipeline externally connected with the storage bottle and is arranged at one end of the pipeline far away from the storage bottle, and the flow of the gas mixture discharged through the pipeline is regulated and controlled through the first control valve;

the pressure control and pressing part is connected with the first control valve through a pipeline, the pressure control and pressing part comprises a vacuum generator, the vacuum generator is connected with the first control valve through a pipeline, and the pressure in the pipeline connected between the vacuum generator and the first control valve is adjusted to be in a negative pressure state through the vacuum generator.

2. A device for the prevention of pipeline blockage according to claim 1, wherein said device for the prevention of pipeline blockage comprises a first flow measuring member mounted on a pipe provided between said storage bottle and said first control valve, said first flow measuring member having an inlet and an outlet, said inlet and said filling port of said storage bottle communicating with each other, and the flow rate of said gas mixture discharged from said filling port of said storage bottle is detected by said first flow measuring member.

3. The device for preventing pipeline blockage according to claim 2, wherein the vacuum generator has an air inlet, a vacuum port and an air outlet, and further comprises an air compression assembly, the air compression assembly comprises an air compression member, the air compression member is communicated with the air inlet formed on the vacuum generator through a pipeline, and the air compression member compresses the outside air.

4. The apparatus for removing nitrogen oxides as claimed in claim 3, wherein the control member further comprises a second control valve disposed on the line between the vacuum generator and the first control valve.

5. The device for removing nitrogen capable of preventing pipeline blockage according to claim 3 or 4, wherein the control pressure part further comprises a third control valve, the third control valve is arranged at the position, close to the air inlet, of the vacuum generator, and the opening and the closing of the air inlet are controlled through the third control valve.

6. The apparatus for removing oxygen and nitrogen as claimed in claim 5, wherein the control member further comprises a fourth control valve, the fourth control valve is disposed near the outlet of the vacuum generator, and the fourth control valve controls the opening and closing of the outlet.

7. The device for removing oxygen and nitrogen capable of preventing pipeline blockage according to claim 6, wherein the air compression assembly further comprises a fifth control valve, the fifth control valve is arranged on a pipeline arranged between the air compression element and the vacuum generator, and the opening and the closing of the air compression element are controlled through the fifth control valve.

8. The device for removing oxygen and nitrogen capable of preventing pipeline blockage according to claim 7, wherein the flow control assembly further comprises a second flow measuring element, the second flow measuring element is arranged on the pipeline arranged between the air compression element and the vacuum generator, and the flow of the compressed air introduced into the vacuum generator from the air compression element is detected through the second flow measuring element.

9. The apparatus for preventing blockage of a pipeline in a deoxynitrogen plant according to claim 8, further comprising a pressure measuring module, wherein the pressure measuring module comprises a pressure measuring member, the pressure measuring member is arranged on a pipeline arranged between the first control valve and the vacuum generator, and the pressure value in the pipeline arranged between the first control valve and the vacuum generator is detected through the pressure measuring member.

10. The device for preventing pipeline blockage according to claim 1, further comprising a thermostatic element, wherein the thermostatic element is disposed in the storage bottle and can be heated.

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