CN220878303U - Tail gas purifier for zirconium-hafnium separation process - Google Patents

Tail gas purifier for zirconium-hafnium separation process Download PDF

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Publication number
CN220878303U
CN220878303U CN202322766934.3U CN202322766934U CN220878303U CN 220878303 U CN220878303 U CN 220878303U CN 202322766934 U CN202322766934 U CN 202322766934U CN 220878303 U CN220878303 U CN 220878303U
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tail gas
fixedly connected
container
plate
pipe
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CN202322766934.3U
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毕延春
孙海虹
臧伟荣
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Nantong Jingpeng New Material Technology Co ltd
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Nantong Jingpeng New Material Technology Co ltd
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Abstract

The utility model discloses a tail gas purifier for zirconium-hafnium separation process, which relates to the technical field of tail gas purification and comprises the following components: the device comprises a processing container, wherein a top cover is fixedly connected to the upper portion of the processing container, a first pressurizing pump and a second pressurizing pump are fixedly arranged on the top cover, an air inlet pipe is fixedly connected to the lower portion of the processing container, an exhaust pipe is fixedly connected to the upper portion of the processing container, a solution tank communicated with each other is fixedly connected to the lower portion of the processing container, and a first extracting pipe is fixedly connected between the first pressurizing pump and the solution tank. Through the mutual cooperation of the first plate-type container, the second plate-type container, the first nozzle group and the second nozzle group, the absorption capacity of the treatment solution at different heights can be guaranteed to be the same, and the tail gas treatment capacity is guaranteed to be good, so that the tail gas treatment efficiency is improved, meanwhile, the double spraying is carried out, the contact area of the tail gas and the solution is further increased, and the tail gas treatment effect is guaranteed to be good and the use is convenient.

Description

Tail gas purifier for zirconium-hafnium separation process
Technical Field
The utility model relates to the technical field of tail gas purification, in particular to a tail gas purifier for a zirconium-hafnium separation process.
Background
In the zirconium-hafnium separation process, tail gas containing peculiar smell can be generated, and the tail gas can be continuously discharged after being purified, so that a tail gas purifier is needed.
In the prior art, tail gas treatment is usually carried out by spraying corresponding treatment solution to remove peculiar smell in tail gas, but a spray head is usually arranged at the top, and the treatment solution can absorb molecules in the tail gas in the falling process and is saturated, so that the treatment effect at the bottom is affected, the treatment efficiency is lower, and the use is inconvenient.
Disclosure of utility model
In order to overcome the defects of the prior art, one of the purposes of the utility model is to provide a tail gas purifier for a zirconium-hafnium separation process, which can ensure that the absorption capacity of treatment solutions with different heights is the same and the tail gas treatment capacity is good through the mutual matching of a plate-type container I, a plate-type container II, a spray head group I and a spray head group II, thereby improving the tail gas treatment efficiency, simultaneously, the tail gas treatment efficiency is improved, the contact area between the tail gas and the solution is further increased by double spraying, the tail gas treatment effect is good, and the use is convenient.
One of the purposes of the utility model is realized by adopting the following technical scheme: the utility model provides a tail gas purifier of zirconium hafnium separation technology, includes the treatment container, the upper portion fixedly connected with top cap of treatment container, fixedly mounted has force (forcing) pump first, force (forcing) pump second on the top cap, the lower part fixedly connected with intake pipe of treatment container, the upper portion fixedly connected with blast pipe of treatment container, the lower part fixedly connected with of treatment container is the solution case of intercommunication each other, fixedly connected with extraction pipe first between force (forcing) pump and the solution case, fixedly connected with extraction pipe second between force (forcing) pump second and the solution case, the inside fixedly connected with connecting plate first of treatment container, fixedly connected with plate type container first on the connecting plate, be provided with shower nozzle group first on the plate type container first, the inside fixedly connected with connecting plate second of treatment container, fixedly connected with plate type container second on the connecting plate type container, be provided with shower nozzle group second on the plate type container second, the output of force (forcing) pump first and plate type container intercommunication, the output of force (forcing) pump second is linked together with plate type container first. Through the mutual cooperation of the first plate-type container, the second plate-type container, the first nozzle group and the second nozzle group, the absorption capacity of the treatment solution at different heights can be guaranteed to be the same, and the tail gas treatment capacity is guaranteed to be good, so that the tail gas treatment efficiency is improved, meanwhile, the double spraying is carried out, the contact area of the tail gas and the solution is further increased, and the tail gas treatment effect is guaranteed to be good and the use is convenient.
According to the tail gas purifier of the zirconium-hafnium separation process, the air inlet pipe is fixedly connected with the air inlet flange, and the air inlet pipe is higher than the solution tank.
According to the tail gas purifier of the zirconium-hafnium separation process, the exhaust pipe is fixedly connected with an exhaust flange, and the exhaust pipe is higher than the plate-type container I.
According to the tail gas purifier of the zirconium-hafnium separation process, the first plate-type container and the second plate-type container are oppositely arranged.
According to the tail gas purifier of the zirconium-hafnium separation process, the plate-type container I and the plate-type container II are both arranged higher than the solution tank.
According to the tail gas purifier of the zirconium-hafnium separation process, the plate-type container I and the plate-type container II are the same in size.
According to the tail gas purifier of the zirconium-hafnium separation process, the solution tank is provided with a liquid adding pipe and a liquid outlet pipe, and the liquid adding pipe is higher than the liquid outlet pipe.
According to the tail gas purifier of the zirconium-hafnium separation process, the first connecting plate and the second connecting plate are arranged in an axisymmetric mode.
Advantageous effects
Compared with the prior art, the utility model discloses a plate container one that sets up, plate container two, shower nozzle group one, shower nozzle group two mutually support, can guarantee that the treatment solution absorbing capacity of not co-altitude is the same, guarantee that the ability of handling tail gas is good to improve tail gas treatment's efficiency, simultaneously, dual spraying, further increase tail gas and solution's area of contact, guarantee that tail gas treatment effect is good, convenient to use.
Additional aspects and advantages of the utility model 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 utility model.
Drawings
The utility model is further described below with reference to the drawings and examples;
FIG. 1 is a schematic diagram of a tail gas purifier for a zirconium hafnium separation process according to the present utility model;
FIG. 2 is a schematic structural view of an exhaust gas purifier according to another aspect of the zirconium hafnium separation process of the present utility model;
FIG. 3 is a schematic diagram showing the structure of the tail gas purifier according to the present utility model in a lower view angle;
Fig. 4 is a schematic diagram of the internal structure of the tail gas purifier of the zirconium hafnium separation process according to the present utility model.
Legend description:
1. A processing container; 2. a top cover; 3. a pressurizing pump I; 4. a second pressurizing pump; 5. an air inlet flange; 6. an air inlet pipe; 7. an extraction pipe II; 8. an extraction pipe I; 9. a solution tank; 10. an exhaust pipe; 11. an exhaust flange; 12. a first plate-type container; 13. a first connecting plate; 14. a first nozzle group; 15. a second nozzle group; 16. a second connecting plate; 17. and a second plate-type container.
Detailed Description
Reference will now be made in detail to the present embodiments of the present utility model, examples of which are illustrated in the accompanying drawings, wherein the accompanying drawings are used to supplement the description of the written description so that one can intuitively and intuitively understand each technical feature and overall technical scheme of the present utility model, but not to limit the scope of the present utility model.
Referring to fig. 1-4, the tail gas purifier for the zirconium hafnium separation process of the embodiment of the utility model comprises a processing container 1, wherein a top cover 2 is fixedly connected to the upper part of the processing container 1, a pressurizing pump I3 and a pressurizing pump II 4 are fixedly arranged on the top cover 2, an air inlet pipe 6 is fixedly connected to the air inlet pipe 6, an air inlet flange 5 is fixedly connected to the air inlet pipe 6 and is higher than a solution tank 9, an exhaust pipe 10 is fixedly connected to the upper part of the processing container 1, an exhaust flange 11 is fixedly connected to the exhaust pipe 10, the exhaust pipe 10 is higher than a plate-type container I12, a solution tank 9 which is communicated with each other is fixedly connected to the lower part of the processing container 1, a liquid adding pipe and a liquid outlet pipe are arranged on the solution tank 9, a pumping pipe 8 is fixedly connected between the first pressurizing pump I3 and the solution tank 9, a pumping pipe II 4 is fixedly connected to the solution tank 9, a pumping pipe II 7 is fixedly connected between the pressurizing pump II 4 and the solution tank 9, a connecting plate I13 is fixedly connected to the inside the processing container 1, the connecting plate I13 and the air inlet pipe 6 is arranged in an axisymmetric manner, the upper part of the connecting plate I13 is fixedly connected to the plate I12, an exhaust pipe 10 is fixedly connected to the upper part of the processing container I12, an exhaust pipe 10 is fixedly connected to the plate-type container 12, an exhaust pipe 11 is fixedly connected to the plate I12, a plate-type container 17 is arranged opposite to the plate-type container 17, the upper end of the plate I17 is fixedly connected to the connecting plate II, the plate II is connected to the plate II, the two containers 17 is connected to the upper end of the two containers 17, and is connected to the two containers are connected to the upper end of the container 17, which is connected to the upper container 17, and is connected to the upper container 17. Through the mutual cooperation of the plate-type container I, the plate-type container II 12, the spray head group I14 and the spray head group II 15, the same absorption capacity of treatment solutions with different heights can be ensured, and the tail gas treatment capacity is ensured to be good, so that the tail gas treatment efficiency is improved, meanwhile, the double spraying is performed, the contact area of the tail gas and the solution is further increased, the tail gas treatment effect is ensured to be good, and the use is convenient.
Working principle: when the tail gas treatment device is used, external tail gas enters from the air inlet pipe 6 and enters the treatment container 1, the first pressurizing pump 3 and the second pressurizing pump 4 pump the treatment solution of the solution tank 9 through the first pumping pipe 8 and the second pumping pipe 7, then the treatment solution is respectively conveyed into the first plate-type container 12 and the second plate-type container 17, and then sprayed out through the first spray head group 14 and the second spray head group 15, the treatment solution is fully contacted with the tail gas, the same absorption capacity of the treatment solution at different heights can be ensured, the tail gas treatment capacity is ensured to be good, so that the tail gas treatment efficiency is improved, the treated solution flows back into the solution tank 9 again and is then put into use again, and after the treatment solution is saturated, the treatment solution can be discharged and a new treatment solution is replaced.
The embodiments of the present utility model have been described in detail with reference to the accompanying drawings, but the present utility model is not limited to the above embodiments, and various changes can be made within the knowledge of one of ordinary skill in the art without departing from the spirit of the present utility model.

Claims (8)

1. The tail gas purifier for the zirconium hafnium separation process comprises a treatment container (1), and is characterized in that a top cover (2) is fixedly connected to the upper portion of the treatment container (1), a first pressurizing pump (3) and a second pressurizing pump (4) are fixedly installed on the top cover (2), an air inlet pipe (6) is fixedly connected to the lower portion of the treatment container (1), an exhaust pipe (10) is fixedly connected to the upper portion of the treatment container (1), a solution tank (9) which is mutually communicated is fixedly connected to the lower portion of the treatment container (1), a first extracting pipe (8) is fixedly connected between the first pressurizing pump (3) and the solution tank (9), a second extracting pipe (7) is fixedly connected between the second pressurizing pump (4) and the solution tank (9), a first connecting plate (13) is fixedly connected to the inner portion of the treatment container (1), a first plate-type container (12) is fixedly connected to the connecting plate-type container (12), a first nozzle group (14) is arranged on the inner portion of the treatment container (1), a second connecting plate (16) is fixedly connected to the inner portion of the treatment container (1), a first pressurizing pipe (17) is fixedly connected to the second connecting plate (17), a second connecting plate-type container (17) is fixedly connected to the first connecting plate (17), a second connecting plate-type container (17) is fixedly connected to the second connecting plate (17), the output end of the second pressurizing pump (4) is communicated with the first plate-type container (12).
2. The tail gas purifier for the zirconium hafnium separation process according to claim 1, wherein the air inlet pipe (6) is fixedly connected with an air inlet flange (5), and the air inlet pipe (6) is higher than the solution tank (9).
3. The tail gas purifier for the zirconium hafnium separation process according to claim 1, wherein an exhaust flange (11) is fixedly connected to the exhaust pipe (10), and the exhaust pipe (10) is higher than the plate-type container I (12).
4. The tail gas purifier for the zirconium hafnium separation process according to claim 1, wherein the first plate container (12) is disposed opposite to the second plate container (17).
5. The tail gas purifier for the zirconium hafnium separation process according to claim 1, wherein the first plate container (12) and the second plate container (17) are arranged higher than the solution tank (9).
6. The tail gas purifier for the zirconium hafnium separation process according to claim 1, wherein the first plate container (12) and the second plate container (17) are the same in size.
7. The tail gas purifier for the zirconium hafnium separation process according to claim 1, wherein a liquid adding pipe and a liquid outlet pipe are arranged on the solution tank (9), and the liquid adding pipe is higher than the liquid outlet pipe.
8. The tail gas purifier for the zirconium hafnium separation process according to claim 1, wherein the first connecting plate (13) and the second connecting plate (16) are axially symmetrically arranged.
CN202322766934.3U 2023-10-16 2023-10-16 Tail gas purifier for zirconium-hafnium separation process Active CN220878303U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202322766934.3U CN220878303U (en) 2023-10-16 2023-10-16 Tail gas purifier for zirconium-hafnium separation process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202322766934.3U CN220878303U (en) 2023-10-16 2023-10-16 Tail gas purifier for zirconium-hafnium separation process

Publications (1)

Publication Number Publication Date
CN220878303U true CN220878303U (en) 2024-05-03

Family

ID=90866687

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202322766934.3U Active CN220878303U (en) 2023-10-16 2023-10-16 Tail gas purifier for zirconium-hafnium separation process

Country Status (1)

Country Link
CN (1) CN220878303U (en)

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