CN210825418U - A system device for recycling and reusing industrial waste hydrogen - Google Patents

A system device for recycling and reusing industrial waste hydrogen Download PDF

Info

Publication number
CN210825418U
CN210825418U CN201921543360.0U CN201921543360U CN210825418U CN 210825418 U CN210825418 U CN 210825418U CN 201921543360 U CN201921543360 U CN 201921543360U CN 210825418 U CN210825418 U CN 210825418U
Authority
CN
China
Prior art keywords
water
tank
pipe
compressor
fixed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201921543360.0U
Other languages
Chinese (zh)
Inventor
孙丽华
张树生
孙桐
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fushun Yifang New Material Co ltd
Original Assignee
Fushun Yifang New Material Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fushun Yifang New Material Co ltd filed Critical Fushun Yifang New Material Co ltd
Priority to CN201921543360.0U priority Critical patent/CN210825418U/en
Application granted granted Critical
Publication of CN210825418U publication Critical patent/CN210825418U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Landscapes

  • Separation Of Gases By Adsorption (AREA)

Abstract

本实用新型公开了一种对工业废氢气回收再利用的系统装置,包括处理箱,处理箱的左侧设有生产箱,处理箱内部的底面固定有气液分离罐和冷冻盐水换热器,且气液分离罐位于冷冻盐水换热器的左侧,处理箱内部的底面右侧固定有过滤分离器,处理箱内部的底面固定有吸附塔和水箱,且水箱位于吸附塔的左侧,生产箱内通过进气管连接在处理箱内气液分离罐的进气口,气液分离罐的出气口通过第一管道依次连接在冷冻盐水换热器、过滤分离器和吸附塔的内部,吸附塔上侧的出气口通过第一管道连接在支管的内部,支管固定在处理箱的底面,且支管位于水箱的左侧,该对工业废氢气回收再利用的系统装置操作简单、循环利用、能源利用效率高。

Figure 201921543360

The utility model discloses a system device for recycling and reusing industrial waste hydrogen, which comprises a treatment box, a production box is arranged on the left side of the treatment box, and a gas-liquid separation tank and a frozen brine heat exchanger are fixed on the bottom surface of the inside of the treatment box. And the gas-liquid separation tank is located on the left side of the frozen brine heat exchanger, a filter separator is fixed on the right side of the bottom surface inside the processing tank, an adsorption tower and a water tank are fixed on the bottom surface inside the processing tank, and the water tank is located on the left side of the adsorption tower. The inside of the box is connected to the air inlet of the gas-liquid separation tank in the treatment box through the air inlet pipe, and the air outlet of the gas-liquid separation tank is connected to the inside of the chilled brine heat exchanger, the filter separator and the adsorption tower in turn through the first pipeline. The air outlet on the upper side is connected to the inside of the branch pipe through the first pipe, the branch pipe is fixed on the bottom surface of the treatment tank, and the branch pipe is located on the left side of the water tank. efficient.

Figure 201921543360

Description

一种对工业废氢气回收再利用的系统装置A system device for recycling and reusing industrial waste hydrogen

技术领域technical field

本实用新型涉及节能减排中的废氢气再利用技术领域,具体为一种对工业废氢气回收再利用的系统装置。The utility model relates to the technical field of waste hydrogen recycling in energy saving and emission reduction, in particular to a system device for recycling and recycling industrial waste hydrogen.

背景技术Background technique

常温常压下,氢气是一种极易燃烧,无色透明、无臭无味的气体,医学上用氢气来治疗疾病,在化工业也被广泛应用,在一些化工设备运行过程中,由于氢气中含有杂质,因此这些含有杂质的氢气被排放到空气中,这样不仅对生态环境造成严重的破坏,而且浪费了氢资源,从而增加了原料成本,而现有的处理费氢气的方法,通常使用物理吸附的方法,但这种方法由于吸附剂本身的特性,吸附效果有限,而且需要经常更换吸附材料,从而提高了劳动成本。Under normal temperature and pressure, hydrogen is an extremely flammable, colorless, transparent, odorless and tasteless gas. It is used in medicine to treat diseases and is also widely used in the chemical industry. It contains impurities, so these hydrogen containing impurities are discharged into the air, which not only causes serious damage to the ecological environment, but also wastes hydrogen resources, thereby increasing the cost of raw materials. However, this method has limited adsorption effect due to the characteristics of the adsorbent itself, and requires frequent replacement of the adsorbent material, thereby increasing the labor cost.

实用新型内容Utility model content

本实用新型要解决的技术问题是克服现有的缺陷,提供一种对工业废氢气回收再利用的系统装置,操作简单、循环利用、能源利用效率高,可以有效解决背景技术中的问题。The technical problem to be solved by the utility model is to overcome the existing defects and provide a system device for recycling and reusing industrial waste hydrogen, which has simple operation, recycling and high energy utilization efficiency, and can effectively solve the problems in the background technology.

为实现上述目的,本实用新型提供如下技术方案:一种对工业废氢气回收再利用的系统装置,包括处理箱,所述处理箱的左侧设有生产箱,所述处理箱内部的底面固定有气液分离罐和冷冻盐水换热器,且气液分离罐位于冷冻盐水换热器的左侧,所述处理箱内部的底面右侧固定有过滤分离器,所述处理箱内部的底面固定有吸附塔和水箱,且水箱位于吸附塔的左侧,所述生产箱内通过进气管连接在处理箱内气液分离罐的进气口,所述气液分离罐的出气口通过第一管道依次连接在冷冻盐水换热器、过滤分离器和吸附塔的内部,所述吸附塔上侧的出气口通过第一管道连接在支管的内部,所述支管固定在处理箱的底面,且支管位于水箱的左侧,所述冷冻盐水换热器底侧的出气口通过第二管道依次与过滤分离器和吸附塔的内部连通,所述吸附塔底侧的出气口通过第二管道与水箱的内部连通,所述支管的出气口通过出气管与生产箱的内部连通,所述气液分离罐的前侧固定有第一压缩机,所述第一压缩机的排气口与气液分离罐的内部连通,所述第一压缩机的输入端电连接单片机的输出端,所述处理箱的前侧固定有单片机,所述单片机的输入端电连接外部电源的输出端,生产箱内含有杂质的氢气通过进气管进入气液分离罐内,气液分离罐分离掉含有杂质的氢气中的机械液滴,通过第一压缩机加压,使含有杂质的氢气通过第一管道进入冷冻盐水换热器内,冷冻盐水换热器将温度冷却,从而使氢气中大量的杂质分离,冷冻盐水换热器内的氢气通过第一管道进入过滤分离器和吸附塔内,再通过第一管道、支管和出气管进入生产箱内循环使用,冷冻盐水换热器内含有少量杂质的氢气通过第二管道进入过滤分离器内部,通过过滤分离器将氢气中少量的杂质分离,过滤分离器内含有少量的杂质的氢气通过第二管道进入吸附塔内,吸附塔吸附氢气中的少量杂质,剩余的氢气再通过第二管道进入水箱内进一步处理。In order to achieve the above purpose, the present utility model provides the following technical solutions: a system device for recycling industrial waste hydrogen gas, comprising a treatment box, a production box is arranged on the left side of the treatment box, and the bottom surface inside the treatment box is fixed There are a gas-liquid separation tank and a frozen brine heat exchanger, and the gas-liquid separation tank is located on the left side of the frozen brine heat exchanger, a filter separator is fixed on the right side of the bottom surface inside the processing box, and the bottom surface inside the processing box is fixed There is an adsorption tower and a water tank, and the water tank is located on the left side of the adsorption tower. The production box is connected to the air inlet of the gas-liquid separation tank in the processing box through the air inlet pipe, and the air outlet of the gas-liquid separation tank passes through the first pipeline. Connected to the inside of the frozen brine heat exchanger, the filter separator and the adsorption tower in turn, the air outlet on the upper side of the adsorption tower is connected to the inside of the branch pipe through the first pipeline, the branch pipe is fixed on the bottom surface of the treatment box, and the branch pipe is located in the On the left side of the water tank, the air outlet on the bottom side of the chilled brine heat exchanger is communicated with the filter separator and the interior of the adsorption tower in turn through the second pipeline, and the air outlet on the bottom side of the adsorption tower is connected with the interior of the water tank through the second pipeline. The air outlet of the branch pipe is communicated with the inside of the production box through the air outlet pipe, the front side of the gas-liquid separation tank is fixed with a first compressor, and the exhaust port of the first compressor is connected to the gas-liquid separation tank Internally connected, the input end of the first compressor is electrically connected to the output end of the single-chip microcomputer, the front side of the processing box is fixed with a single-chip microcomputer, the input end of the single-chip microcomputer is electrically connected to the output end of the external power supply, and the production box contains impurities. The hydrogen enters the gas-liquid separation tank through the intake pipe, and the gas-liquid separation tank separates the mechanical droplets in the hydrogen containing impurities, and is pressurized by the first compressor, so that the hydrogen containing impurities enters the frozen brine heat exchanger through the first pipeline Inside, the chilled brine heat exchanger cools the temperature, so that a large amount of impurities in the hydrogen are separated. The hydrogen in the chilled brine heat exchanger enters the filter separator and adsorption tower through the first pipeline, and then passes through the first pipeline, branch pipes and outlet. The gas pipe enters the production box for recycling, and the hydrogen containing a small amount of impurities in the frozen brine heat exchanger enters the filter separator through the second pipeline, and the small amount of impurities in the hydrogen is separated by the filter separator. The filter separator contains a small amount of impurities. The hydrogen enters the adsorption tower through the second pipeline, the adsorption tower absorbs a small amount of impurities in the hydrogen, and the remaining hydrogen enters the water tank through the second pipeline for further processing.

进一步的,还包括抽水管、进水管、高压喷头和水泵,所述水箱的后侧固定有水泵,所述水泵的进水口通过抽水管与水箱的出水口连通,所述水泵的出水口通过进水管与水箱的进水口连通,所述进水管靠近水箱内的一端连接有高压喷头,所述水泵的输入端电连接单片机的输出端,水泵通过抽水管将水箱内的水抽出,再通过进水管和高压喷头喷进水箱内,使氢气中剩余的杂质溶于水。Further, it also includes a water suction pipe, a water inlet pipe, a high-pressure nozzle and a water pump, a water pump is fixed on the rear side of the water tank, the water inlet of the water pump is connected with the water outlet of the water tank through the water suction pipe, and the water outlet of the water pump is connected with the water inlet of the water tank. The water pipe is communicated with the water inlet of the water tank, the end of the water inlet pipe close to the water tank is connected with a high-pressure nozzle, the input end of the water pump is electrically connected to the output end of the single-chip microcomputer, and the water pump draws out the water in the water tank through the water pumping pipe, and then passes through the water inlet pipe. And the high-pressure nozzle is sprayed into the water tank, so that the remaining impurities in the hydrogen are dissolved in water.

进一步的,还包括第二压缩机和第三导管,所述水箱内部的左侧固定有第二压缩机,所述第二压缩机的排气口通过第三导管与第一管道的内部连通,所述第二压缩机的输入端电连接单片机的输出端,当杂质溶于水后,第二压缩机加压,剩余的少量氢气通过第三导管进入第一管道内,再通过支管和出气管进入生产箱内循环使用。Further, it also includes a second compressor and a third conduit, a second compressor is fixed on the left side of the inside of the water tank, and the exhaust port of the second compressor is communicated with the interior of the first pipeline through the third conduit, The input end of the second compressor is electrically connected to the output end of the single-chip microcomputer. When the impurities are dissolved in water, the second compressor is pressurized, and the remaining small amount of hydrogen enters the first pipeline through the third conduit, and then passes through the branch pipe and the gas outlet pipe. Into the production box for recycling.

进一步的,还包括防回流阀门,所述第三导管的侧面设有防回流阀门,防回流阀门防止剩余的少量氢气回流到水箱内,从而防止氢气的二次污染。Further, a backflow prevention valve is also included, and a backflow prevention valve is provided on the side of the third conduit. The backflow prevention valve prevents the remaining small amount of hydrogen from flowing back into the water tank, thereby preventing secondary pollution of hydrogen.

进一步的,还包括第二阀门和第一阀门,所述进气管的侧面设有第一阀门,所述出气管的侧面设有第二阀门,第二阀门和第一阀门方便控制所处理含有杂质的氢气的量,使反应更完全。Further, it also includes a second valve and a first valve, the side of the air inlet pipe is provided with a first valve, the side of the air outlet pipe is provided with a second valve, and the second valve and the first valve are convenient to control the impurities that are processed. amount of hydrogen to make the reaction more complete.

与现有技术相比,本实用新型的有益效果是:本对工业废氢气回收再利用的系统装置,具有以下好处:Compared with the prior art, the beneficial effects of the present utility model are: the system device for recycling and reusing industrial waste hydrogen has the following advantages:

1、通过设置水箱,对吸附塔内含有少量杂质的氢气进一步处理,通过设置高压喷头,增大了杂质与水的接触面积,使氢气中的杂质更易溶于水,使回收的氢气纯度更高。1. By setting a water tank, the hydrogen containing a small amount of impurities in the adsorption tower is further processed. By setting a high-pressure nozzle, the contact area between impurities and water is increased, so that the impurities in the hydrogen are more soluble in water, and the purity of the recovered hydrogen is higher. .

2、通过低温分离和变温吸附的方法,操作简单、所用成本低、回收效率高。2. The method of low temperature separation and temperature swing adsorption has the advantages of simple operation, low cost and high recovery efficiency.

3、通过整个装置对废氢气的回收处理,循环利用,减少了含有杂质的氢气的排放,避免了资源的浪费,减轻了对大气污染的伤害。3. Through the recovery and recycling of waste hydrogen by the whole device, the discharge of hydrogen containing impurities is reduced, the waste of resources is avoided, and the damage to air pollution is reduced.

附图说明Description of drawings

图1为本实用新型结构示意图;Fig. 1 is the structural representation of the utility model;

图2为本实用新型左侧结构示意图;Fig. 2 is the structural representation of the left side of the utility model;

图中:1处理箱、2生产箱、3进气管、4气液分离罐、5冷冻盐水换热器、6过滤分离器、7吸附塔、8第一压缩机、9水箱、10抽水管、11进水管、12高压喷头、13水泵、14第二压缩机、15单片机、16第三导管、17防回流阀门、18出气管、19第二阀门、20第一阀门、21第一管道、22第二管道、23支管。In the picture: 1 processing box, 2 production box, 3 intake pipe, 4 gas-liquid separation tank, 5 frozen brine heat exchanger, 6 filter separator, 7 adsorption tower, 8 first compressor, 9 water tank, 10 water pump, 11 water inlet pipe, 12 high pressure nozzle, 13 water pump, 14 second compressor, 15 single chip microcomputer, 16 third conduit, 17 backflow prevention valve, 18 air outlet pipe, 19 second valve, 20 first valve, 21 first pipeline, 22 The second pipeline, 23 branch pipes.

具体实施方式Detailed ways

下面将结合本实用新型实施例中的附图,对本实用新型实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本实用新型一部分实施例,而不是全部的实施例。基于本实用新型中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本实用新型保护的范围。The technical solutions in the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model. Obviously, the described embodiments are only a part of the embodiments of the present utility model, rather than all the implementations. example. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the protection scope of the present invention.

请参阅图1-2,本实用新型提供一种技术方案:一种对工业废氢气回收再利用的系统装置,包括处理箱1,处理箱1的左侧设有生产箱2,处理箱1内部的底面固定有气液分离罐4和冷冻盐水换热器5,且气液分离罐4位于冷冻盐水换热器5的左侧,处理箱1内部的底面右侧固定有过滤分离器6,处理箱1内部的底面固定有吸附塔7和水箱9,且水箱9位于吸附塔7的左侧,生产箱2内通过进气管3连接在处理箱1内气液分离罐4的进气口,气液分离罐4的出气口通过第一管道21依次连接在冷冻盐水换热器5、过滤分离器6和吸附塔7的内部,吸附塔7上侧的出气口通过第一管道21连接在支管23的内部,支管23固定在处理箱1的底面,且支管23位于水箱9的左侧,冷冻盐水换热器5底侧的出气口通过第二管道22依次与过滤分离器6和吸附塔7的内部连通,吸附塔7底侧的出气口通过第二管道22与水箱9的内部连通,支管23的出气口通过出气管18与生产箱2的内部连通,气液分离罐4的前侧固定有第一压缩机8,第一压缩机8的排气口与气液分离罐4的内部连通,还包括第二阀门19和第一阀门20,进气管3的侧面设有第一阀门20,出气管18的侧面设有第二阀门19,第二阀门19和第一阀门20方便控制所处理含有杂质的氢气的量,使反应更完全,生产箱2内含有杂质的氢气通过进气管3进入气液分离罐4内,气液分离罐4分离掉含有杂质的氢气中的机械液滴,通过第一压缩机8加压,使含有杂质的氢气通过第一管道21进入冷冻盐水换热器5内,冷冻盐水换热器5将温度冷却,从而使氢气中大量的杂质分离,冷冻盐水换热器5内的氢气通过第一管道21进入过滤分离器6和吸附塔7内,再通过第一管道21、支管23和出气管18进入生产箱2内循环使用,冷冻盐水换热器5内含有少量杂质的氢气通过第二管道22进入过滤分离器6内部,通过过滤分离器6将氢气中少量的杂质分离,过滤分离器6内含有少量的杂质的氢气通过第二管道22进入吸附塔7内,吸附塔7吸附氢气中的少量杂质,剩余的氢气再通过第二管道22进入水箱9内进一步处理,还包括抽水管10、进水管11、高压喷头12和水泵13,水箱9的后侧固定有水泵13,水泵13的进水口通过抽水管10与水箱9的出水口连通,水泵13的出水口通过进水管11与水箱9的进水口连通,进水管11靠近水箱内的一端连接有高压喷头12,水泵13通过抽水管10将水箱9内的水抽出,再通过进水管11和高压喷头12喷进水箱9内,使氢气中剩余的杂质溶于水,还包括第二压缩机14和第三导管16,水箱9内部的左侧固定有第二压缩机14,第二压缩机14的排气口通过第三导管16与第一管道21的内部连通,当杂质溶于水后,第二压缩机14加压,剩余的少量氢气通过第三导管16进入第一管道21内,再通过支管23和出气管18进入生产箱2内循环使用,还包括防回流阀门17,第三导管16的侧面设有防回流阀门17,防回流阀门17防止剩余的少量氢气回流到水箱9内,从而防止氢气的二次污染。Please refer to FIGS. 1-2 , the present utility model provides a technical solution: a system device for recycling industrial waste hydrogen, including a treatment box 1 , a production box 2 is arranged on the left side of the treatment box 1 , and inside the treatment box 1 A gas-liquid separation tank 4 and a frozen brine heat exchanger 5 are fixed on the bottom surface of the tank, and the gas-liquid separation tank 4 is located on the left side of the frozen brine heat exchanger 5, and a filter separator 6 is fixed on the right side of the bottom surface inside the treatment box 1. The bottom surface of the box 1 is fixed with an adsorption tower 7 and a water tank 9, and the water tank 9 is located on the left side of the adsorption tower 7. The production box 2 is connected to the air inlet of the gas-liquid separation tank 4 in the processing box 1 through the air inlet pipe 3. The air outlet of the liquid separation tank 4 is sequentially connected to the inside of the chilled brine heat exchanger 5, the filter separator 6 and the adsorption tower 7 through the first pipeline 21, and the air outlet on the upper side of the adsorption tower 7 is connected to the branch pipe 23 through the first pipeline 21. Inside, the branch pipe 23 is fixed on the bottom surface of the treatment tank 1, and the branch pipe 23 is located on the left side of the water tank 9, and the air outlet on the bottom side of the chilled brine heat exchanger 5 is connected to the filter separator 6 and the adsorption tower 7 through the second pipeline 22 in turn. Internal communication, the air outlet on the bottom side of the adsorption tower 7 is communicated with the interior of the water tank 9 through the second pipeline 22, the air outlet of the branch pipe 23 is communicated with the interior of the production box 2 through the air outlet pipe 18, and the front side of the gas-liquid separation tank 4 is fixed with a The first compressor 8, the exhaust port of the first compressor 8 is communicated with the interior of the gas-liquid separation tank 4, and also includes a second valve 19 and a first valve 20, the side of the intake pipe 3 is provided with a first valve 20, and the outlet is provided with a first valve 20. The side of the gas pipe 18 is provided with a second valve 19, the second valve 19 and the first valve 20 are convenient to control the amount of hydrogen containing impurities to be processed, so that the reaction is more complete, and the hydrogen containing impurities in the production box 2 enters the gas through the intake pipe 3. In the liquid separation tank 4, the gas-liquid separation tank 4 separates the mechanical droplets in the hydrogen containing impurities, and is pressurized by the first compressor 8, so that the hydrogen containing impurities enters the frozen brine heat exchanger 5 through the first pipeline 21 , the chilled brine heat exchanger 5 cools the temperature, so that a large amount of impurities in the hydrogen are separated, and the hydrogen in the chilled brine heat exchanger 5 enters the filter separator 6 and the adsorption tower 7 through the first pipeline 21, and then passes through the first pipeline. 21. The branch pipe 23 and the gas outlet pipe 18 enter the production box 2 for recycling. The hydrogen containing a small amount of impurities in the frozen brine heat exchanger 5 enters the filter separator 6 through the second pipeline 22, and a small amount of hydrogen is removed through the filter separator 6. Impurity separation, the hydrogen containing a small amount of impurities in the filter separator 6 enters the adsorption tower 7 through the second pipeline 22, the adsorption tower 7 absorbs a small amount of impurities in the hydrogen, and the remaining hydrogen enters the water tank 9 through the second pipeline 22 for further processing , also includes a water pumping pipe 10, a water inlet pipe 11, a high-pressure nozzle 12 and a water pump 13, a water pump 13 is fixed on the rear side of the water tank 9, and the water inlet of the water pump 13 is communicated with the water outlet of the water tank 9 through the water pumping pipe 10, and the water outlet of the water pump 13 The water inlet pipe 11 is communicated with the water inlet of the water tank 9. One end of the water inlet pipe 11 close to the water tank is connected with a high-pressure nozzle 12. Inlet tank 9 Inside, the remaining impurities in the hydrogen are dissolved in water, and the second compressor 14 and the third conduit 16 are also included. The left side of the water tank 9 is fixed with a second compressor 14. The three conduits 16 are communicated with the interior of the first conduit 21. When the impurities are dissolved in water, the second compressor 14 is pressurized, and the remaining small amount of hydrogen enters the first conduit 21 through the third conduit 16, and then passes through the branch pipe 23 and the gas outlet pipe. 18 enters the production tank 2 for recycling, and also includes an anti-reflux valve 17. The side of the third conduit 16 is provided with an anti-reflux valve 17. The anti-reflux valve 17 prevents the remaining small amount of hydrogen from flowing back into the water tank 9, thereby preventing the secondary hydrogen Pollution.

其中,还包括单片机15,处理箱1的前侧固定有单片机15,单片机15的输入端电连接外部电源的输出端,单片机15的输出端电连接第一压缩机8、第二压缩机14和水泵13的输入端。The single-chip microcomputer 15 is also included. The front side of the processing box 1 is fixed with a single-chip microcomputer 15. The input end of the single-chip microcomputer 15 is electrically connected to the output end of the external power supply. The input end of the water pump 13 .

在使用时:打开单片机15和第一阀门20,生产箱2内含有杂质的氢气通过进气管3进入气液分离罐4内,气液分离罐4分离掉含有杂质的氢气中的机械液滴,通过第一压缩机8加压,使含有杂质的氢气通过第一管道21进入冷冻盐水换热器5内,冷冻盐水换热器5将温度冷却,从而使氢气中大量的杂质分离,冷冻盐水换热器5内的氢气通过第一管道21进入过滤分离器6和吸附塔7内,再通过第一管道21、支管23和出气管18进入生产箱2内循环使用,冷冻盐水换热器5内含有少量杂质的氢气通过第二管道22进入过滤分离器6内部,通过过滤分离器6将氢气中少量的杂质分离,过滤分离器6内含有少量的杂质的氢气通过第二管道22进入吸附塔7内,吸附塔7吸附氢气中的少量杂质,剩余的氢气再通过第二管道22进入水箱9内,水泵13通过抽水管10将水箱9内的水抽出,再通过进水管11和高压喷头12喷进水箱9内,使氢气中剩余的杂质溶于水,当杂质溶于水后,第二压缩机14加压,剩余的少量氢气通过第三导管16进入第一管道21内,再通过支管23和出气管18进入生产箱2内循环使用,防回流阀门17防止剩余的少量氢气回流到水箱9内,从而防止氢气的二次污染,第二阀门19和第一阀门20方便控制所处理含有杂质的氢气的量,使反应更完全。When in use: open the single chip 15 and the first valve 20, the hydrogen containing impurities in the production box 2 enters the gas-liquid separation tank 4 through the air inlet pipe 3, and the gas-liquid separation tank 4 separates the mechanical droplets in the hydrogen containing impurities, Pressurized by the first compressor 8, the hydrogen containing impurities enters the frozen brine heat exchanger 5 through the first pipeline 21, and the frozen brine heat exchanger 5 cools the temperature, so that a large amount of impurities in the hydrogen are separated, and the frozen brine exchange The hydrogen in the heater 5 enters the filter separator 6 and the adsorption tower 7 through the first pipe 21, and then enters the production box 2 through the first pipe 21, the branch pipe 23 and the gas outlet pipe 18 for recycling. The hydrogen containing a small amount of impurities enters the inside of the filter separator 6 through the second pipeline 22, a small amount of impurities in the hydrogen are separated by the filter separator 6, and the hydrogen containing a small amount of impurities in the filter separator 6 enters the adsorption tower 7 through the second pipeline 22 Inside, the adsorption tower 7 adsorbs a small amount of impurities in the hydrogen, and the remaining hydrogen enters the water tank 9 through the second pipeline 22. In the water inlet tank 9, the remaining impurities in the hydrogen are dissolved in water. When the impurities are dissolved in water, the second compressor 14 is pressurized, and the remaining small amount of hydrogen enters the first pipeline 21 through the third conduit 16, and then passes through the branch pipe. 23 and the gas outlet pipe 18 enter the production tank 2 for recycling, the anti-return valve 17 prevents the remaining small amount of hydrogen from flowing back into the water tank 9, thereby preventing the secondary pollution of hydrogen, and the second valve 19 and the first valve 20 are convenient to control the processing containing The amount of impurity hydrogen makes the reaction more complete.

值得注意的是,本实施例中所公开的单片机15,具体型号为德州仪器TMS370,第一压缩机8、第二压缩机14和水泵13则可根据实际应用场景自由配置,第一压缩机8、第二压缩机14可选用谷轮压缩机,具体型号为ZR61KC-TFD-522,水泵13可选用酷龙水泵,具体型号为JET-G17-37,单片机15控制第一压缩机8、第二压缩机14和水泵13工作采用现有技术中常用的方法。It is worth noting that the specific model of the single-chip microcomputer 15 disclosed in this embodiment is Texas Instruments TMS370, and the first compressor 8, the second compressor 14 and the water pump 13 can be freely configured according to actual application scenarios. The first compressor 8 , The second compressor 14 can choose the Copeland compressor, the specific model is ZR61KC-TFD-522, the water pump 13 can choose the Kulong water pump, the specific model is JET-G17-37, the microcontroller 15 controls the first compressor 8, the second compressor The operation of the compressor 14 and the water pump 13 adopts the methods commonly used in the prior art.

尽管已经示出和描述了本实用新型的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本实用新型的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本实用新型的范围由所附权利要求及其等同物限定。Although the embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes and modifications can be made to these embodiments without departing from the principles and spirit of the present invention , alternatives and modifications, the scope of the present invention is defined by the appended claims and their equivalents.

Claims (5)

1.一种对工业废氢气回收再利用的系统装置,其特征在于:包括处理箱(1),所述处理箱(1)的左侧设有生产箱(2),所述处理箱(1)内部的底面固定有气液分离罐(4)和冷冻盐水换热器(5),且气液分离罐(4)位于冷冻盐水换热器(5)的左侧,所述处理箱(1)内部的底面右侧固定有过滤分离器(6),所述处理箱(1)内部的底面固定有吸附塔(7)和水箱(9),且水箱(9)位于吸附塔(7)的左侧,所述生产箱(2)内通过进气管(3)连接在处理箱(1)内气液分离罐(4)的进气口,所述气液分离罐(4)的出气口通过第一管道(21)依次连接在冷冻盐水换热器(5)、过滤分离器(6)和吸附塔(7)的内部,所述吸附塔(7)上侧的出气口通过第一管道(21)连接在支管(23)的内部,所述支管(23)固定在处理箱(1)的底面,且支管(23)位于水箱(9)的左侧,所述冷冻盐水换热器(5)底侧的出气口通过第二管道(22)依次与过滤分离器(6)和吸附塔(7)的内部连通,所述吸附塔(7)底侧的出气口通过第二管道(22)与水箱(9)的内部连通,所述支管(23)的出气口通过出气管(18)与生产箱(2)的内部连通,所述气液分离罐(4)的前侧固定有第一压缩机(8),所述第一压缩机(8)的排气口与气液分离罐(4)的内部连通,所述第一压缩机(8)的输入端电连接单片机(15)的输出端,所述处理箱(1)的前侧固定有单片机(15),所述单片机(15)的输入端电连接外部电源的输出端。1. A system device for recycling industrial waste hydrogen gas, characterized in that: comprising a treatment box (1), the left side of the treatment box (1) is provided with a production box (2), the treatment box (1) ) inside the bottom surface is fixed with a gas-liquid separation tank (4) and a frozen brine heat exchanger (5), and the gas-liquid separation tank (4) is located on the left side of the frozen brine heat exchanger (5), and the treatment box (1 ) is fixed with a filter separator (6) on the right side of the bottom surface of the interior, and an adsorption tower (7) and a water tank (9) are fixed on the bottom surface of the treatment box (1), and the water tank (9) is located at the bottom of the adsorption tower (7). On the left side, the production box (2) is connected to the air inlet of the gas-liquid separation tank (4) in the processing box (1) through the air inlet pipe (3), and the air outlet of the gas-liquid separation tank (4) passes through The first pipeline (21) is sequentially connected to the inside of the frozen brine heat exchanger (5), the filter separator (6) and the adsorption tower (7), and the air outlet on the upper side of the adsorption tower (7) passes through the first pipeline ( 21) Connected to the inside of the branch pipe (23), the branch pipe (23) is fixed on the bottom surface of the processing tank (1), and the branch pipe (23) is located on the left side of the water tank (9), and the frozen brine heat exchanger (5) ) The air outlet on the bottom side is communicated with the interior of the filter separator (6) and the adsorption tower (7) through the second pipeline (22) in turn, and the air outlet on the bottom side of the adsorption tower (7) is connected through the second pipeline (22) It is communicated with the interior of the water tank (9), the air outlet of the branch pipe (23) is communicated with the interior of the production box (2) through the air outlet pipe (18), and the front side of the gas-liquid separation tank (4) is fixed with a first A compressor (8), the exhaust port of the first compressor (8) is communicated with the inside of the gas-liquid separation tank (4), and the input end of the first compressor (8) is electrically connected to the single-chip microcomputer (15) An output end, a single chip (15) is fixed on the front side of the processing box (1), and an input end of the single chip (15) is electrically connected to an output end of an external power supply. 2.根据权利要求1所述的一种对工业废氢气回收再利用的系统装置,其特征在于:还包括抽水管(10)、进水管(11)、高压喷头(12)和水泵(13),所述水箱(9)的后侧固定有水泵(13),所述水泵(13)的进水口通过抽水管(10)与水箱(9)的出水口连通,所述水泵(13)的出水口通过进水管(11)与水箱(9)的进水口连通,所述进水管(11)靠近水箱内的一端连接有高压喷头(12),所述水泵(13)的输入端电连接单片机(15)的输出端。2. A system device for recycling and reusing industrial waste hydrogen gas according to claim 1, characterized in that: it also comprises a water pumping pipe (10), a water inlet pipe (11), a high-pressure nozzle (12) and a water pump (13) , a water pump (13) is fixed on the rear side of the water tank (9), the water inlet of the water pump (13) is communicated with the water outlet of the water tank (9) through the suction pipe (10), and the outlet of the water pump (13) The water inlet is communicated with the water inlet of the water tank (9) through a water inlet pipe (11), and one end of the water inlet pipe (11) close to the water tank is connected with a high-pressure nozzle (12), and the input end of the water pump (13) is electrically connected to the single-chip microcomputer ( 15) at the output. 3.根据权利要求2所述的一种对工业废氢气回收再利用的系统装置,其特征在于:还包括第二压缩机(14)和第三导管(16),所述水箱(9)内部的左侧固定有第二压缩机(14),所述第二压缩机(14)的排气口通过第三导管(16)与第一管道(21)的内部连通,所述第二压缩机(14)的输入端电连接单片机(15)的输出端。3. A system device for recycling industrial waste hydrogen gas according to claim 2, characterized in that: it further comprises a second compressor (14) and a third conduit (16), and the inside of the water tank (9) A second compressor (14) is fixed on the left side of the second compressor (14), the discharge port of the second compressor (14) communicates with the inside of the first pipe (21) through a third conduit (16), the second compressor (14) The input end of (14) is electrically connected to the output end of the microcontroller (15). 4.根据权利要求3所述的一种对工业废氢气回收再利用的系统装置,其特征在于:还包括防回流阀门(17),所述第三导管(16)的侧面设有防回流阀门(17)。4. A system device for recycling industrial waste hydrogen gas according to claim 3, characterized in that: further comprising a backflow prevention valve (17), and a backflow prevention valve is provided on the side of the third conduit (16) (17). 5.根据权利要求1所述的一种对工业废氢气回收再利用的系统装置,其特征在于:还包括第二阀门(19)和第一阀门(20),所述进气管(3)的侧面设有第一阀门(20),所述出气管(18)的侧面设有第二阀门(19)。5. A system device for recycling industrial waste hydrogen gas according to claim 1, characterized in that: further comprising a second valve (19) and a first valve (20), the A first valve (20) is provided on the side surface, and a second valve (19) is provided on the side surface of the air outlet pipe (18).
CN201921543360.0U 2019-09-17 2019-09-17 A system device for recycling and reusing industrial waste hydrogen Expired - Fee Related CN210825418U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921543360.0U CN210825418U (en) 2019-09-17 2019-09-17 A system device for recycling and reusing industrial waste hydrogen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921543360.0U CN210825418U (en) 2019-09-17 2019-09-17 A system device for recycling and reusing industrial waste hydrogen

Publications (1)

Publication Number Publication Date
CN210825418U true CN210825418U (en) 2020-06-23

Family

ID=71272819

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201921543360.0U Expired - Fee Related CN210825418U (en) 2019-09-17 2019-09-17 A system device for recycling and reusing industrial waste hydrogen

Country Status (1)

Country Link
CN (1) CN210825418U (en)

Similar Documents

Publication Publication Date Title
CN204402891U (en) A kind of energy saving and environment friendly Roots vacuum system
CN210825418U (en) A system device for recycling and reusing industrial waste hydrogen
CN211837274U (en) A natural gas purification and desulfurization system
CN206295767U (en) A kind of Sucralose production solvent recovering system
CN210699439U (en) A device for the production of reagent sulfuric acid to remove SO2
CN205867912U (en) Novel tail gas is retrieved device
CN211274202U (en) Medium-sized dichlorosilane tail gas treatment and absorption device
CN210674716U (en) A fatty alcohol waste gas treatment system
CN209286983U (en) A kind of improved VOC recovery system
CN221763955U (en) Energy-saving clean vacuum circulating cooling system
CN223936229U (en) Nitrogen separation and recovery equipment for tire vulcanization
CN204678301U (en) A kind of steam regeneration energy conserving system
CN211770762U (en) A high-efficiency industrial waste acid water treatment equipment
CN220003524U (en) Hydrochloric acid tail gas absorption treatment device
CN221905823U (en) Vacuum treatment device
CN217887468U (en) Diffusion furnace tail gas collecting device
CN210057809U (en) Exhaust gas treatment device for dimethomorph
CN223484886U (en) Steam condensate recovery device
CN214944863U (en) Large-traffic vacuum pump combination equipment
CN220664890U (en) Purifying device for ultrapure hydrogen
CN219433825U (en) Vacuum pump air extractor
CN204469667U (en) A kind of vacuum system for the production of silicone sealant
CN204625506U (en) Useless time sodium liquid reclaims acetylene gas process unit
CN203484029U (en) Tail gas recovery treatment device
CN205784672U (en) A kind of device for recovering steam condensing water

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20200623

CF01 Termination of patent right due to non-payment of annual fee