阅读说明：本技术 一种槽罐恒压控制系统 (Tank constant pressure control system ) 是由 裴陆军 吴海东 于 2020-04-30 设计创作，主要内容包括：本发明公开一种槽罐恒压控制系统,包括槽罐、供氮组件和水封阻火罐,槽罐的排气端和供氮组件的供氮管路并联至水封阻火罐的气体连接管,水封阻火罐的内部设有上水封层和下水封层,气体连接管顶端延伸至上水封层顶面,气体连接管顶端用于与槽罐的排气端和供氮组件的供氮管路连通,且上水封层用于与应急负压管路连通,气体连接管底端延伸至下水封层内,气体连接管底端用于与VOCs收集管连通。本申请公开的槽罐恒压控制系统,在槽罐的排气端设置水封阻火罐,利用水封阻火罐下水封层控制槽罐排液时槽罐内部压力恒定,通过水封阻火罐上水封层和应急负压管路控制系统出现故障时槽罐内部压力,可有效确保密闭槽罐的压力稳定性,提高了密闭槽罐的安全性。(The invention discloses a constant pressure control system for a tank, which comprises the tank, a nitrogen supply assembly and a water-sealed fire-resisting tank, wherein an exhaust end of the tank and a nitrogen supply pipeline of the nitrogen supply assembly are connected in parallel to a gas connecting pipe of the water-sealed fire-resisting tank, an upper water seal layer and a lower water seal layer are arranged inside the water-sealed fire-resisting tank, the top end of the gas connecting pipe extends to the top surface of the upper water seal layer, the top end of the gas connecting pipe is used for being communicated with the exhaust end of the tank and the nitrogen supply pipeline of the nitrogen supply assembly, the upper water seal layer is used for being communicated with an emergency negative pressure pipeline, the bottom end of the gas connecting pipe extends into the lower water seal layer. The application discloses tank constant voltage control system sets up the water seal at the exhaust end of tank and hinders the cupping jar, utilizes water seal back-fire relief jar lower water seal control tank flowing back time slot jar internal pressure invariable, hinders cupping jar upper water seal and emergent negative pressure pipeline control system through water seal and breaks down time slot jar internal pressure, can effectively ensure the pressure stability of airtight tank, has improved the security of airtight tank.)

1. A constant pressure control system of a tank is characterized by comprising a tank (1), a nitrogen supply component (2) and a water seal fire retardant tank (3), the exhaust end of the tank (1) and the nitrogen supply pipeline of the nitrogen supply component (2) are connected in parallel to the gas connecting pipe (301) of the water-sealed fire-blocking tank (3), an upper water seal layer (302) and a lower water seal layer (303) are arranged inside the water-sealed fire-blocking tank (3), the top end of the gas connecting pipe (301) extends to the top surface of the upper water seal layer (302), the top end of the gas connecting pipe (301) is communicated with the exhaust end of the tank (1) and the nitrogen supply pipeline of the nitrogen supply component (2), and the upper water seal layer (302) is used for being communicated with the emergency negative pressure pipeline (4), the bottom end of the gas connecting pipe (301) extends into the lower water seal layer (303), the bottom end of the gas connecting pipe (301) is used for being communicated with a VOCs collecting pipe (5).

2. The tank constant pressure control system according to claim 1, wherein the water-sealed fire-blocking tank (3) further comprises a water supply port (304) and a liquid discharge port (305), the water supply port (304) is used for replenishing the upper water seal layer (302) and the lower water seal layer (303) with liquid, and the liquid discharge port (305) is arranged at the side of the water-sealed fire-blocking tank (3).

3. The constant pressure tank control system as claimed in claim 2, wherein the bottom of the water-sealed fire-blocking tank (3) is further provided with a sewage draining outlet (306).

4. Tank constant pressure control system according to claim 3, characterized in that the pipe connection height of the emergency negative pressure pipe (4) is greater than the sealed liquid level height of the lower water seal (303).

5. The tank constant pressure control system according to claim 4, wherein the height of the liquid discharge port (305) is greater than the sealed liquid level of the lower water seal layer (303).

6. The tank constant pressure control system according to claim 5, wherein the sealed liquid level height value of the lower water seal layer (303) is 150mm to 300 mm.

7. The tank constant pressure control system according to any one of claims 1 to 6, wherein the nitrogen supply assembly (2) comprises an electric shut-off valve (201), a flow control valve (202), a pressure regulating valve (203) and a bypass line (204), the electric shut-off valve (201) is interlocked with a start signal of a drain pump (101) of the tank (1), the flow control valve (202) is arranged at an exhaust end of the nitrogen supply line, and the pressure regulating valve (203) and the bypass line (204) are connected in parallel and are arranged between the electric shut-off valve (201) and the flow control valve (202).

8. The tank constant pressure control system according to claim 7, wherein the pressure regulating valve (203) is a self-standing pressure regulating valve.

Technical Field

The invention relates to the technical field of metallurgical equipment, in particular to a constant-pressure control system for a tank.

Background

The closed chemical tank is affected by the material inlet and outlet, the gas volatilized by the internal medium is allowed to be discharged or sucked into a certain amount of gas, when the tank is internally provided with flammable, explosive and volatile media, the gas discharged from the internal part has explosion risks when meeting fire or high temperature, and the VOC gas generated by the media is extremely difficult to dispose.

At present, the most ideal method is to carry out combustion treatment after collection, the existing VOCs gas collection device is generally a closed tank, when the closed tank belongs to flammable, explosive and volatile media, the exhaust gas inside the closed tank has explosion risks when encountering fire or high temperature, therefore, the VOCs gas collection method provides a serious test for the safety of the closed tank, the safety of the closed tank is difficult to guarantee by adopting a general control method of a breather valve for control, and meanwhile, for the extremely volatile liquid, the breather valve control accelerates the volatilization of the liquid due to large pressure fluctuation, wastes materials and brings certain difficulty for subsequent treatment.

Therefore, how to solve the problem that the internal pressure of the closed tank is unstable due to the control of the internal pressure of the closed tank by the breather valve is a technical problem to be solved urgently by those skilled in the art.

Disclosure of Invention

The invention aims to provide a constant-pressure control system for a tank, which realizes constant-pressure control on a closed tank by arranging a water seal layer, can effectively ensure the pressure stability of the closed tank, effectively controls the quantity of VOCs gas volatilized by a volatile medium, and improves the safety of the closed tank.

In order to solve the technical problem, the invention provides a constant pressure control system for a tank, which comprises the tank, a nitrogen supply assembly and a water-sealed fire-blocking tank, wherein an exhaust end of the tank and a nitrogen supply pipeline of the nitrogen supply assembly are connected in parallel to a gas connecting pipe of the water-sealed fire-blocking tank, an upper water seal layer and a lower water seal layer are arranged inside the water-sealed fire-blocking tank, the top end of the gas connecting pipe extends to the top surface of the upper water seal layer, the top end of the gas connecting pipe is communicated with the exhaust end of the tank and the nitrogen supply pipeline of the nitrogen supply assembly, the upper water seal layer is communicated with an emergency negative pressure pipeline, the bottom end of the gas connecting pipe extends into the lower water seal layer, and the bottom end of the gas connecting pipe is communicated with a VOCs collecting pipe.

Preferably, the water-sealed fire-blocking tank further comprises a water supply port and a liquid discharge port, the water supply port is used for supplementing the liquid of the upper water sealing layer and the lower water sealing layer, and the liquid discharge port is arranged on the side edge of the water-sealed fire-blocking tank.

Preferably, a sewage draining outlet is further formed in the bottom of the water-sealed fire retardant tank.

Preferably, the height of a connecting pipe of the emergency negative pressure pipeline is greater than the height of the sealed liquid level of the lower water seal layer.

Preferably, the height of the liquid outlet is greater than the height of the sealed liquid level of the lower water seal layer.

Preferably, the height value of the sealed liquid level of the lower water sealing layer is 150 mm-300 mm.

Preferably, the nitrogen supply assembly comprises an electric cut-off valve, a flow control valve, a pressure regulating valve and a bypass pipeline, the electric cut-off valve is interlocked with a starting signal of a liquid discharge pump of the tank, the flow control valve is arranged at an exhaust end of the nitrogen supply pipeline, and the pressure regulating valve is connected with the bypass pipeline in parallel and is arranged between the electric cut-off valve and the flow control valve.

Preferably, the pressure regulating valve is a self-standing pressure regulating valve.

The invention provides a constant pressure control system for a tank, which comprises the tank, a nitrogen supply assembly and a water-sealed fire-resisting tank, wherein an exhaust end of the tank and a nitrogen supply pipeline of the nitrogen supply assembly are connected in parallel to a gas connecting pipe of the water-sealed fire-resisting tank, an upper water seal layer and a lower water seal layer are arranged inside the water-sealed fire-resisting tank, the top end of the gas connecting pipe extends to the top surface of the upper water seal layer, the top end of the gas connecting pipe is used for being communicated with the exhaust end of the tank and the nitrogen supply pipeline of the nitrogen supply assembly, the upper water seal layer is used for being communicated with an emergency negative pressure pipeline, the bottom end of the gas connecting pipe extends into the lower water seal layer. The application discloses tank constant voltage control system sets up the water seal through the exhaust end at the tank and hinders the cupping jar, utilizes the lower water seal control tank flowing back time slot jar internal pressure of water seal to hinder cupping jar invariable to through the last water seal of water seal and emergent negative pressure pipeline control system time slot jar internal pressure that breaks down, can effectively ensure the pressure stability of airtight tank, improved the security of airtight tank.

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 embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the provided drawings without creative efforts.

FIG. 1 is a schematic overall structure diagram of an embodiment of the present invention;

fig. 2 is a schematic structural view of the water-sealing fire retardant tank shown in fig. 1.

Wherein, in fig. 1-2:

the device comprises a tank-1, a liquid discharge pump-101, a nitrogen supply assembly-2, an electric cut-off valve-201, a flow control valve-202, a pressure regulating valve-203, a bypass pipeline-204, a water seal fire-blocking tank-3, a gas connecting pipe-301, an upper water seal layer-302, a lower water seal layer-303, a water supply opening-304, a liquid discharge opening-305, a sewage discharge opening-306, an emergency negative pressure pipeline-4 and a VOCs collecting pipe-5.

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.

Referring to fig. 1 and 2, fig. 1 is a schematic overall structure diagram of an embodiment of the present invention; fig. 2 is a schematic structural view of the water-sealing fire retardant tank shown in fig. 1. Wherein the arrows in the figure indicate the gas or liquid flow direction.

In a specific embodiment provided by the invention, the device mainly comprises a tank 1, a nitrogen supply component 2 and a water-seal fire-retardant tank 3, wherein an exhaust end of the tank 1 and a nitrogen supply pipeline of the nitrogen supply component 2 are connected in parallel to a gas connecting pipe 301 of the water-seal fire-retardant tank 3, an upper water seal layer 302 and a lower water seal layer 303 are arranged inside the water-seal fire-retardant tank 3, the top end of the gas connecting pipe 301 extends to the top surface of the upper water seal layer 302, the top end of the gas connecting pipe 301 is used for being communicated with the exhaust end of the tank 1 and the nitrogen supply pipeline of the nitrogen supply component 2, the upper water seal layer 302 is used for being communicated with an emergency negative pressure pipeline 4, the bottom end of the gas connecting pipe 301 extends into the lower water seal layer 303, and the bottom end of the gas.

Wherein, tank 1 is the gaseous collection device of VOCs, tank 1's exhaust end and the confession nitrogen pipeline that supplies nitrogen subassembly 2 connect in parallel to water seal back-fire relief jar 3's gas connection pipe 301, supply nitrogen subassembly 2 to be used for aerifing tank 1 when tank 1 outside flowing back in order to guarantee that tank 1 internal pressure is invariable, gas connection pipe 301 top is used for keeping constant with tank 1's exhaust end and the confession nitrogen pipeline that supplies nitrogen subassembly 2, and water seal back-fire relief jar 3's last water seal 302 and emergent negative pressure pipeline 4 intercommunication are used for adjusting tank 1 internal pressure when tank 1 is inside to present the negative pressure, water seal back-fire relief jar 3's lower water seal 303 is used for adjusting tank 1 internal pressure when tank 1 internal pressure is too big.

Specifically, in the practical application process, when the tank 1 discharges liquid outwards, the liquid discharge pump 101 of the tank 1 is started, the liquid in the tank 1 gradually falls, the gas pressure in the tank 1 also gradually falls, at this time, because the nitrogen supply component 2 is linked with the liquid discharge pump 101 through signals, the nitrogen supply component 2 starts to supply nitrogen to the tank 1, the nitrogen supply component 2 can ensure that the nitrogen supply amount to the tank 1 is slightly larger than the flow rate of the liquid discharge pump 101 according to the flow rate of the liquid discharge pump 101, because the nitrogen supply amount of the nitrogen supply component 2 is slightly larger than the flow rate of the liquid discharge pump 101, the pressure in the tank 1 is always in a positive pressure state, at this time, the pressure in the tank 1 can apply pressure to the liquid in which the lower water seal layer 303 of the water seal fire-arresting tank 3 is in the gas connection pipe 301, and the height at which the gas connection pipe 301 is submerged in the lower water seal layer 303, that is the pressure received by the water seal height h3 of the lower water seal layer, thereby realizing constant pressure in the tank 1; when liquid is fed into the tank 1, the nitrogen supply assembly 2 does not charge nitrogen into the tank 1, the pressure of gas in the tank 1 is gradually increased along with the gradual increase of the liquid, and when the pressure in the tank 1 is greater than the pressure received by the water sealing height h3 of the lower water sealing layer 303, the gas in the tank 1 naturally breaks through the lower water sealing layer 303 and is discharged to reduce the pressure in the tank 1, so that the pressure in the tank 1 is always kept at the pressure received by the water sealing height h3 of the lower water sealing layer 303, and the constant pressure in the tank 1 is realized.

In order to optimize the advantage that the constant pressure control system of the tank can ensure the more stable internal pressure of the tank 1 and the advantage that the operation is simpler in the middle of the above-mentioned embodiment, the water seal fire retardant tank 3 further comprises a water supply port 304 and a liquid discharge port 305, the water supply port 304 is used for supplementing the liquid of the upper water seal layer 302 and the lower water seal layer 303, and the liquid discharge port 305 is arranged at the side of the water seal fire retardant tank 3. In the actual process of controlling the constant pressure, because the pressure of the tank 1 is controlled by the water seal, the water supply opening 304 can perform water filling operation on the upper water sealing layer 302 and the lower water sealing layer 303 of the water seal fire-retardant tank 3 to ensure the normal operation of a pressure constant system, meanwhile, when liquid is fed into the tank 1, gas breaks through the lower water sealing layer 303 to discharge the gas, in the process, the water of the lower water sealing layer 303 splashes out, so that the water quantity of the lower water sealing layer 303 is reduced, and the water quantity of the lower water sealing layer 303 can be supplemented by the water supply opening 304 to ensure the pressure control effect; the drain port 305 is provided on the side of the water sealing and fire blocking tank 3 for draining the excess water and the water splashed out of the water sealing layer 303.

It should be noted that a sewage draining outlet 306 is also arranged at the bottom of the water-sealed fire-retardant tank 3. Because of the reason of the tank 1 working environment, some impurities possibly entering the inside of the water seal fire-retarding tank 3 can be discharged through the sewage outlet 306, and the optimization of the working environment of the water seal fire-retarding tank 3 is ensured.

It should be noted that the height h1 of the connecting pipe of the emergency negative pressure pipeline 4 is greater than the height h3 of the sealed liquid level of the lower water seal layer 303; the height value of the sealed liquid level h3 of the lower water seal layer 303 is generally designed to be 150 mm-300 mm. When the nitrogen supply amount of the nitrogen supply assembly 2 is not matched with the liquid discharge volume of the tank 1, when the nitrogen supply amount of the nitrogen supply assembly 2 is smaller than the liquid discharge amount, negative pressure is gradually formed in the tank 1, when the negative pressure is greater than the liquid level h2 sealed by the upper water seal layer 302 of the water-sealed fire-blocking tank 3, the atmospheric pressure breaks through the liquid level h2 sealed by the upper water seal layer 302, and the atmospheric pressure enters the tank, so that the pressure of the tank 1 is ensured not to be lower than the pressure of the liquid level h2 sealed by the upper water seal layer 302; because the water-seal exhaust pipe is connected with the VOCs collecting pipe 5, when the pipeline of the VOCs collecting pipe 5 is abnormal and the collecting pipeline is in positive pressure, the gas pressure discharged by the tank 1 is controlled by the height h1 of the connecting pipe of the emergency negative pressure pipeline 4, and the height h1 of the connecting pipe of the emergency negative pressure pipeline 4 is slightly larger than the water sealing height h3 of the lower water seal layer 303, so that the pressure of the tank 1 is controlled; when the pipelines of the VOCs collecting pipes 5 are abnormal or sporadic sparks are arranged outside the emergency negative pressure pipeline 4, the sparks are isolated by water in the upper water sealing layer 302, so that the safety control of gas in the tank 1 is ensured, and the safety of the tank 1 is ensured.

Further, the height of the liquid outlet 305 is greater than the sealed liquid level of the lower water seal layer 303, since the internal pressure of the tank 1 needs to be maintained within a certain range to ensure the normal operation of the tank 1, and the height h4 of the liquid outlet 305 is slightly greater than the sealed liquid level h3 of the lower water seal layer 303, it can be ensured that the positive pressure gas inside the tank 1 is not discharged when the water seal water is discharged, thereby ensuring the constant internal pressure of the tank 1.

Further, the nitrogen supply assembly 2 comprises an electric cut-off valve 201, a flow control valve 202, a pressure regulating valve 203 and a bypass pipeline 204, the electric cut-off valve 201 is interlocked with a starting signal of the liquid discharge pump 101 of the tank 1, the flow control valve 202 is arranged at the exhaust end of the nitrogen supply pipeline, and the pressure regulating valve 203 and the bypass pipeline 204 are connected in parallel and are arranged between the electric cut-off valve 201 and the flow control valve 202; the pressure regulating valve 203 is a self-standing pressure regulating valve. The electric cut-off valve 201 is interlocked with the starting signal of the liquid discharge pump 101 of the tank 1, so that an air supply pipeline can be effectively opened or cut off, and the constant internal pressure of the tank 1 is ensured; the pressure regulating valve 203 is used for regulating the pressure of the nitrogen pipeline, so that the fluctuation of the internal pressure of the tank 1 due to the influence of the pressure of the nitrogen pipeline is avoided, and the constant internal pressure of the tank 1 is improved; the bypass line 204 is used for emergency opening when the pressure regulating valve 203 fails; the flow control valve 202 is used for controlling the flow of nitrogen entering the tank 1, so that the internal pressure of the tank 1 is controlled, and the internal pressure is ensured to be constant.

To sum up, the groove jar constant voltage control system that this embodiment provided mainly includes the groove jar, supply nitrogen subassembly and water seal fire blocking jar, the exhaust end of groove jar and the gas connection pipe that supplies the nitrogen pipeline of nitrogen subassembly to connect in parallel to water seal fire relief jar, the inside of water seal fire relief jar is equipped with water seal and lower water seal, the gas connection pipe top extends to water seal top surface, the gas connection pipe top is used for the exhaust end with the groove jar and supplies the nitrogen pipeline intercommunication of nitrogen subassembly, and go up the water seal and be used for and emergent negative pressure pipeline intercommunication, the gas connection pipe bottom extends to in the water seal down, the gas connection pipe bottom is used for and VOCs collecting pipe intercommunication. The application discloses tank constant voltage control system sets up the water seal through the exhaust end at the tank and hinders the cupping jar, utilizes the lower water seal control tank flowing back time slot jar internal pressure of water seal to hinder cupping jar invariable to through the last water seal of water seal and emergent negative pressure pipeline control system time slot jar internal pressure that breaks down, can effectively ensure the pressure stability of airtight tank, improved the security of airtight tank.

The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.