CN214485754U - Gas-liquid separation component and system for realizing reaction and filtering concentration reactor - Google Patents
Gas-liquid separation component and system for realizing reaction and filtering concentration reactor Download PDFInfo
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- CN214485754U CN214485754U CN202023278123.1U CN202023278123U CN214485754U CN 214485754 U CN214485754 U CN 214485754U CN 202023278123 U CN202023278123 U CN 202023278123U CN 214485754 U CN214485754 U CN 214485754U
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Abstract
The utility model relates to sewage treatment, in particular to a gas-liquid separation component and a system thereof for realizing a reaction and filtration concentration reactor, wherein the gas-liquid separation component is arranged at the liquid material output end for realizing the reaction and filtration concentration reactor; the gas-liquid separation subassembly includes and is used for realizing two at least vacuum tanks that the liquid output end of reaction and filtration concentration reactor is connected, and the gas output end that sets up on these two at least vacuum tanks is connected with gas delivery house steward, and this gas delivery house steward has circulation tank through water circulation vacuum pump connection, and this circulation tank's liquid delivery end is used for being connected with water circulation vacuum pump through the liquid pump. The at least two vacuum tanks are arranged not only for arranging the spare vacuum tank, but also for performing gas-liquid separation on liquid materials at different times by utilizing time difference, namely a plurality of vacuum tanks, so that the reaction in the reactor can be continuously and continuously performed, and the gas-liquid separation is ensured to be more sufficient.
Description
Technical Field
The utility model relates to a sewage treatment, in particular to a gas-liquid separation subassembly and system for realizing reaction and filtration concentration reactor.
Background
In a process flow in which a reaction raw material is reacted to obtain a reaction product and then the reaction product is filtered and concentrated, a reaction apparatus for reaction and a filtering and concentrating apparatus for filtering and concentrating are usually two different apparatuses independent of each other. For example, in a preparation process of a ternary material precursor of a lithium ion battery, a reaction kettle and a centrifuge are connected with each other, during operation, a mixed salt solution with a certain concentration and a sodium hydroxide solution with a certain concentration, which are prepared from nickel salt (such as nickel sulfate), cobalt salt (such as cobalt sulfate), manganese salt (such as manganese sulfate) and water, respectively enter the reaction kettle and undergo a saline-alkali neutralization reaction in the reaction kettle to generate a ternary material precursor crystal nucleus, and after the reaction is finished, slurry in the reaction kettle is conveyed to the centrifuge for filtration and concentration.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a can be comparatively abundant carry out gas-liquid separation's gas-liquid separation subassembly to the liquid after reaction, concentration.
The technical scheme adopted by the application is that the gas-liquid separation component is used for realizing a reaction and filtering concentration reactor, and is arranged at a liquid material output end of the reaction and filtering concentration reactor; the gas-liquid separation subassembly includes two at least vacuum tanks of being connected with the liquid output that is used for realizing reaction and filtration concentration reactor, and the last liquid material input that sets up of this vacuum tank is connected with the liquid material output that is used for realizing reaction and filtration concentration reactor, and the gas output that sets up on these two at least vacuum tanks is connected with gas delivery house steward, and this gas delivery house steward has circulation tank through water circulation vacuum pump connection, the liquid delivery end of this circulation tank be used for through the liquid pump with water circulation vacuum pump connection.
By arranging the at least two vacuum tanks, not only the standby vacuum tank is arranged, but also the gas-liquid separation can be carried out on the liquid materials at different times by utilizing the time difference, namely, the plurality of vacuum tanks are utilized, so that the reaction in the reactor can be continuously and continuously carried out, the gas-liquid separation is ensured to be more sufficient, and the water circulation vacuum pump can be efficiently operated by arranging the circulating water tank.
Further, the upper end of the vacuum tank is provided with an emptying pipe for releasing gas in the tank.
Furthermore, the upper end of the vacuum tank is provided with a filtering output port with a filter plate for filtering gas in the tank.
Further, the liquid discharge ports of the at least two vacuum tanks are connected with liquid conveying pipes, and the liquid conveying pipes are water-cooling heat exchange pipes.
Further, the vacuum tank is provided with a liquid level sensor, so that the vacuum tank can fully perform gas-liquid separation and monitor the liquid level height of the vacuum tank, and when the liquid in the vacuum tank reaches a threshold value, a valve of a liquid discharge port is opened to discharge the liquid in the vacuum tank.
Furthermore, a cooling interlayer is arranged outside the circulating water tank, and a cooling liquid input end and a waste liquid discharge end are arranged on the cooling interlayer.
The utility model also provides a system for be used for realizing reacting and filtering concentrated reactor, contain foretell gas-liquid separation subassembly that is used for realizing reacting and filtering concentrated reactor.
By adopting the system for realizing the reaction and filtering concentration reactor, the reliability of gas-liquid separation is ensured, and the gas-liquid separation efficiency of the whole system is greatly improved after the circulating water tank is arranged.
Specifically, the liquid material output end of the system for realizing the reaction and filtering concentration reactor is connected with the vacuum tank of the gas-liquid separation component through a pneumatic ball valve and a manual ball valve in sequence.
The liquid material output end for realizing the reaction and filtering concentration reactor is connected with a liquid material output main pipe, liquid material branch pipes with the quantity corresponding to the vacuum tank are respectively arranged on the liquid material output main pipe, and the liquid material branch pipes are connected with the liquid material input end of the vacuum tank.
Specifically, a sleeve is arranged on the liquid material output main pipe.
The power component for realizing a reaction and filtering concentration system can be adopted for providing power (pumping and absorbing) for the gas-liquid separation component, the power component comprises a water circulation vacuum pump, the gas suction end of the water circulation vacuum pump is used for being connected with the gas output end of a vacuum tank for realizing the reaction and filtering concentration system, and the gas exhaust end of the water circulation vacuum pump is connected with a circulating water tank; the input end of the working liquid cavity of the water circulation vacuum pump is communicated with a water circulation pump, the liquid input end of the water circulation pump is communicated with a water circulation tank, and the bottom end of the water circulation tank is provided with a wastewater discharge port.
Through setting up this power component, when the operation, the liquid material carries out gas-liquid separation from a plurality of vacuum tanks from the reactor after, gas is brought into foretell circulation tank by foretell water circulation vacuum pump, wherein, water circulation vacuum pump's process liquid is from foretell circulation tank, from the working solution of part condensate as water circulation vacuum pump in the circulation tank, it is also convenient so that the environmental protection, make entire system compact structure, and through setting up water circulation vacuum pump and above-mentioned circulation pump, the combined action of circulation tank, control the business turn over of three, input/output, the steady and the operation that lasts of nimble guarantee suction.
Furthermore, a cooling interlayer is arranged outside the circulating water tank, and a cooling liquid input end is arranged on the cooling interlayer. The liquid material input into the circulating water tank is condensed, wherein the liquid material comprises the working liquid output from the working liquid cavity of the water circulating vacuum pump, and the loss of the working liquid is also prevented to the maximum extent.
Furthermore, a plurality of cooling liquid input ends arranged along the height direction of the circulating water tank are arranged on the circulating water tank.
Furthermore, the output end of the working liquid cavity of the water circulation vacuum pump is connected with the top end of the circulating water tank.
Further, along the direction from the circulating water pump to the circulating water tank, the pipe diameter of a pipeline for connecting the circulating water pump and the circulating water tank is gradually increased.
The present invention will be further described with reference to the accompanying drawings and the detailed description. Additional aspects and advantages of the invention will be set forth in part in the description which follows and, in part, will be obvious from the description. Or may be learned by practice of the invention.
Drawings
The accompanying drawings, which form a part of the disclosure, are included to assist in understanding the disclosure, and the description provided herein and the accompanying drawings, which are related thereto, are intended to explain the disclosure, but do not constitute an undue limitation on the disclosure.
In the drawings:
FIG. 1 is a schematic diagram illustrating a gas-liquid separation module for carrying out the reaction and filtration concentration reactor according to the present invention;
FIG. 2 is a schematic view for explaining another arrangement of the gas-liquid separation module for carrying out the reaction and filtration concentration reactor according to the present invention;
the labels in the figure are: the device comprises a liquid material input header pipe 1, a vacuum tank 2, a liquid material input end 210, a liquid material branch pipe 211, a gas output end 220, an emptying pipe 230, a filtering output port 240, a liquid conveying pipe 250, a gas conveying header pipe 3, a water circulation vacuum pump 4, a circulating water tank 5, a cooling interlayer 510, a cooling liquid input end 511, a waste water discharge port 520, a liquid level sensor 6 and a circulating water pump 7.
Detailed Description
The present invention will be described more fully with reference to the accompanying drawings. Those of ordinary skill in the art will be able to implement the invention based on these descriptions. Before the present invention is described with reference to the accompanying drawings, it is to be noted that:
the technical solutions and features provided in the present invention in each part including the following description may be combined with each other without conflict.
Moreover, the embodiments of the invention described in the following description are generally only examples of a subset of the invention, and not all examples. Therefore, all other embodiments obtained by a person of ordinary skill in the art without creative efforts based on the embodiments of the present invention shall fall within the protection scope of the present invention.
With respect to the terms and units of the present invention. The term "comprises" and any variations thereof in the description and claims of this invention and the related art are intended to cover non-exclusive inclusions.
Referring to fig. 1, a gas-liquid separation assembly for a reactor for carrying out reaction and filtering concentration is provided at a liquid material output end of the reactor for carrying out reaction and filtering concentration; the gas-liquid separation subassembly includes and is used for realizing two vacuum tanks 2 that the liquid output end of reaction and filtration concentration reactor is connected, the last liquid material input 210 that sets up of this vacuum tank 2 is connected with the liquid material output end that is used for realizing the reaction and filters concentration reactor, liquid material output end is connected with a liquid material input header 1, liquid material input 210 stretches out liquid material branch pipe 211 and connects on this liquid material input header 1, the gas output 220 that sets up on these two vacuum tanks 2 is connected with gas delivery header 3, this gas delivery header 3 is connected with circulation tank 5 through hydrologic cycle vacuum pump 4, the liquid delivery end of this circulation tank 5 be used for through the liquid pump with hydrologic cycle vacuum pump 4 connects. The two vacuum tanks 2 are arranged, a mode that the two vacuum tanks 2 are connected in parallel is adopted, one of the two vacuum tanks can be used as a standby vacuum tank 2, and the gas-liquid separation can be performed on liquid materials at different times by utilizing time difference, so that the reaction in the reactor can be continuously and continuously performed, the gas-liquid separation is ensured to be more sufficient, and the water circulation vacuum pump 4 can be efficiently operated by arranging the circulating water tank 5. The vacuum tank 2 may be provided with various detection instruments such as a thermometer, a humidity detector, a barometer, and the like.
The gas output end 220 of the vacuum tank 2 can be sequentially provided with a pneumatic ball valve and a manual ball valve, and the manual ball valve is arranged behind the pneumatic ball valve so as to ensure the output safety of gas.
The gas outlet 220 may be provided at the uppermost end of the vacuum tank 2, and the liquid inlet 210 may be provided at an upper portion of the side of the vacuum tank 2, that is, the liquid may be introduced from the upper portion of the vacuum tank 2.
The upper end of the vacuum tank 2 is provided with an evacuation pipe 230 for discharging gas in the tank. The evacuation pipe 230 is provided to adjust the air pressure in the vacuum tank 2.
A cooling interlayer 510 is arranged outside the circulating water tank 5, and a cooling liquid input end 511 and a cooling liquid discharge end are arranged on the cooling interlayer 510. Here, a plurality of cooling liquid input terminals 511 may be provided, and the cooling liquid may be introduced into the cooling jacket 510 from different positions, and the cooling liquid may be input to cool and condense the input liquid in the circulation water tank 5, and the cooled and condensed waste liquid may be discharged from the circulation water tank 5.
The upper end of the vacuum tank 2 is provided with a filter outlet 240 with a filter sheet for filtering the gas in the tank. To ensure complete clean drainage, the filter outlet 240 may be provided with removable filter plates, membranes, etc.
The liquid discharge ports of the two vacuum tanks 2 are connected with a liquid delivery pipe 250, and the liquid delivery pipe 250 is a water-cooling heat exchange pipe to ensure that the liquid material output from the vacuum tanks 2 reaches a predetermined temperature and the liquid material has a proper temperature after being separated in the vacuum tanks 2, namely, the temperature of the liquid material in the liquid delivery pipe 250 is controlled.
The vacuum tank 2 is provided with a liquid level sensor 6 so that the vacuum tank 2 can sufficiently perform gas-liquid separation and monitor the liquid level of the vacuum tank 2, and when the liquid in the vacuum tank 2 reaches a threshold value, a valve of a liquid discharge port is opened to discharge the liquid in the vacuum tank 2.
The gas-liquid separation assembly can be used for realizing a system for the reaction and the filtering concentration reactor. By adopting the system for realizing the reaction and filtering concentration reactor, the reliability of gas-liquid separation is ensured, and the gas-liquid separation efficiency of the whole system is greatly improved after the circulating water tank 5 is arranged. And a liquid material output end of a system for realizing the reaction and filtering concentration reactor is connected with the vacuum tank 2 of the gas-liquid separation component sequentially through a pneumatic ball valve and a manual ball valve. Through the series connection of the manual ball valve and the manual ball valve, the safety of liquid material conveying is guaranteed. The liquid material output end is connected with a liquid material output header pipe, liquid material branch pipes 211 of which the number corresponds to that of the vacuum tanks 2 are respectively arranged on the liquid material output header pipe, and the liquid material branch pipes 211 are connected with the liquid material input end 210 of the vacuum tanks 2. When the temperature control device is arranged, a heat-insulating sleeve or a heat-insulating sleeve can be arranged on the liquid material output main pipe so as to ensure that the temperature can be maintained in a stable interval.
The device for providing power for the gas-liquid separation assembly is a power assembly for realizing a reaction and filtration concentration system, the power assembly comprises a water circulation vacuum pump 4, the air suction end of the water circulation vacuum pump 4 is used for being connected with the gas output end 220 of a vacuum tank 2 for realizing the reaction and filtration concentration system, and the air exhaust end of the water circulation vacuum pump 4 is connected with a circulating water tank 5; the input end of the working liquid cavity of the water circulation vacuum pump 4 is communicated with a water circulation pump 7, the liquid input end of the water circulation pump 7 is communicated with a water circulation tank 5, and the bottom end of the water circulation tank 5 is provided with a waste water discharge port 520.
Through the arrangement of the power assembly, during operation, liquid materials are output from the reactor to the plurality of vacuum tanks 2 for gas-liquid separation, and then gas is brought into the circulating water tank 5 by the water circulating vacuum pump 4, wherein process liquid of the water circulating vacuum pump 4 is from the circulating water tank 5, and part of condensate in the circulating water tank 5 is used as working liquid of the water circulating vacuum pump 4, so that the environment is protected, the whole system is compact in structure, and the water circulating vacuum pump 4, the circulating water pump 7 and the circulating water tank 5 are arranged to jointly act, so that the inlet and the outlet, the input and the output of the three are controlled, and stable and continuous pumping operation is flexibly guaranteed.
A cooling interlayer 510 is arranged outside the circulating water tank 5, and a cooling liquid input end 511 is arranged on the cooling interlayer 510. So as to condense the liquid material input into the circulating water tank 5, wherein the liquid material comprises the working fluid output from the working fluid cavity of the water circulating vacuum pump 4, and the loss of the working fluid is maximally prevented. The working fluid of the water circulation vacuum pump 4 described above may be delivered from the gas delivery manifold 3 to the circulation water tank 5, as shown in fig. 2.
The circulation water tank 5 is provided with a plurality of coolant input terminals 511 arranged in the height direction of the circulation water tank 5. Not only can be fast like this fill cooling interlayer 510, also can be fast pour into the coolant liquid into from a plurality of different positions, guarantee refrigerated equilibrium, reduce the cooling inequality that local difference in temperature brought.
The output end of the working liquid cavity of the water circulation vacuum pump 4 is connected with the top end of the circulating water tank 5.
The pipe diameter of the pipeline connecting the circulating water pump 7 and the circulating water tank 5 is gradually increased along the direction from the circulating water pump 7 to the circulating water tank 5.
The contents of the present invention have been explained above. Those of ordinary skill in the art will be able to implement the invention based on these descriptions. Based on the above-mentioned contents of the present invention, all other embodiments obtained by those skilled in the art without creative efforts shall fall within the protection scope of the present invention.
Claims (10)
1. The gas-liquid separation component is used for realizing the reaction and filtering concentration reactor and is characterized in that the gas-liquid separation component is arranged at the liquid material output end of the reactor for realizing the reaction and filtering concentration; the gas-liquid separation subassembly includes two at least vacuum tanks of being connected with the liquid output that is used for realizing reaction and filtration concentration reactor, and the last liquid material input that sets up of this vacuum tank is connected with the liquid material output that is used for realizing reaction and filtration concentration reactor, and the gas output that sets up on these two at least vacuum tanks is connected with gas delivery house steward, and this gas delivery house steward has circulation tank through water circulation vacuum pump connection, the liquid delivery end of this circulation tank be used for through the liquid pump with water circulation vacuum pump connection.
2. The gas-liquid separation module for realizing a reaction and filtering concentration reactor as claimed in claim 1, wherein the upper end of the vacuum tank is provided with a drain pipe for discharging gas in the tank.
3. The gas-liquid separation module for realizing a reaction and filtering concentration reactor as claimed in claim 1, wherein the upper end of the vacuum tank is provided with a filtering output port with a filter plate for filtering gas in the tank.
4. The gas-liquid separation assembly for realizing a reaction and filtering concentration reactor as claimed in claim 1, wherein the liquid discharge ports of the at least two vacuum tanks are connected with liquid delivery pipes, and the liquid delivery pipes are water-cooled heat exchange pipes.
5. The gas-liquid separation assembly for realizing a reaction and filtering concentration reactor as claimed in claim 1, wherein said vacuum tank is provided with a liquid level sensor.
6. The gas-liquid separation assembly for realizing a reaction and filtering concentration reactor as claimed in claim 1, wherein a cooling interlayer is arranged outside the circulating water tank, and a cooling liquid input end and a waste liquid discharge end are arranged on the cooling interlayer.
7. The system for carrying out the reaction and filtering concentration reactor, characterized by comprising the gas-liquid separation assembly for carrying out the reaction and filtering concentration reactor according to any one of claims 1 to 5.
8. The system for realizing a reaction and filtering concentration reactor as claimed in claim 7, wherein the liquid material output end of the system for realizing the reaction and filtering concentration reactor is connected with the vacuum tank of the gas-liquid separation assembly sequentially through a pneumatic ball valve and a manual ball valve.
9. The system for realizing the reaction and filtering concentration reactor according to claim 8, wherein the liquid material output end of the reactor for realizing the reaction and filtering concentration is connected with a liquid material output header pipe, the liquid material output header pipe is respectively provided with a liquid material branch pipe corresponding to the vacuum tank in number, and the liquid material branch pipe is connected with the liquid material input end of the vacuum tank.
10. The system for implementing a reaction and filtration concentration reactor according to claim 9, wherein said liquid feed outlet manifold is provided with a cannula.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023278123.1U CN214485754U (en) | 2020-12-30 | 2020-12-30 | Gas-liquid separation component and system for realizing reaction and filtering concentration reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023278123.1U CN214485754U (en) | 2020-12-30 | 2020-12-30 | Gas-liquid separation component and system for realizing reaction and filtering concentration reactor |
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| Publication Number | Publication Date |
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| CN214485754U true CN214485754U (en) | 2021-10-26 |
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| CN202023278123.1U Active CN214485754U (en) | 2020-12-30 | 2020-12-30 | Gas-liquid separation component and system for realizing reaction and filtering concentration reactor |
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