CN207886908U - Surmount valve adsorption-desorption device - Google Patents

Surmount valve adsorption-desorption device Download PDF

Info

Publication number
CN207886908U
CN207886908U CN201721607735.6U CN201721607735U CN207886908U CN 207886908 U CN207886908 U CN 207886908U CN 201721607735 U CN201721607735 U CN 201721607735U CN 207886908 U CN207886908 U CN 207886908U
Authority
CN
China
Prior art keywords
valve
sub
desorption
adsorption
tower
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.)
Active
Application number
CN201721607735.6U
Other languages
Chinese (zh)
Inventor
椤惧缓
顾建
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.)
SHANGHAI YIJING ENERGY TECHNOLOGY Co Ltd
Original Assignee
SHANGHAI YIJING ENERGY TECHNOLOGY 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 SHANGHAI YIJING ENERGY TECHNOLOGY Co Ltd filed Critical SHANGHAI YIJING ENERGY TECHNOLOGY Co Ltd
Priority to CN201721607735.6U priority Critical patent/CN207886908U/en
Application granted granted Critical
Publication of CN207886908U publication Critical patent/CN207886908U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model provides one kind and surmounting valve adsorption-desorption device, has adsorption-desorption tower A and adsorption-desorption tower B, another that there are two groups to surmount valve, every adsorption-desorption tower has exhaust gas entrance, stripping gas entrance, waste liquid outlet.One end outlet of first group of two sub- valve of absorption for surmounting valve respectively connected the exhaust gas entrance of two adsorption-desorption towers, the other end outlet of this two sub- valves of absorption of both ends difference unicom of the sub- valve of another intercommunication;One end outlet of second group of two sub- valve of desorption for surmounting valve respectively connected the stripping gas entrance of two adsorption-desorption towers, the other end outlet of this two sub- valves of desorption of both ends difference unicom of the sub- valve of another intercommunication.The utilization ratio of two towers of the utility model improves by about one time than the treatment effeciency of traditional parallel double tower, and reduces the error of manual intervention and reduce hand labor intensity.

Description

Surmount valve adsorption-desorption device
Technical field
The utility model is related to the adsorption-desorption devices and its control method of a kind of exhaust gas.
Background technology
In general, the inlet and outlet of the adsorption-desorption device of exhaust gas are connected with various control valve, the valve of different structure With different control modes, the valve of different location has different control actions.
Invention content
Purpose of utility model:
Adsorption-desorption efficiency can be improved by providing one kind, and that reduces the idle waiting time surmounts valve adsorption-desorption device.
Technical solution:
It is described in the utility model to surmount valve adsorption-desorption tower, there is adsorption-desorption tower A and adsorption-desorption tower B, separately have Two groups surmount valve(Every group surmount valve with three combination control sub- valve or similar to the control with three valves And make-break capacity).
Every adsorption-desorption tower has exhaust gas entrance(Enter adsorption-desorption tower for exhaust gas), stripping gas entrance(For stripping gas Body enters adsorption-desorption tower), also waste liquid outlet(For the waste liquid outflow formed after desorption).
One end outlet of first group of surmount valve two sub- valve of absorption respectively connected the useless of two adsorption-desorption towers Gas entrance, the other end outlet of this two sub- valves of absorption of both ends difference unicom of the sub- valve of another intercommunication;Second group surmounts One end outlet of two sub- valves of desorption of valve respectively connected the stripping gas entrance of two adsorption-desorption towers, another intercommunication The other end outlet of this two sub- valves of desorption of both ends difference unicom of sub- valve.
Also there is every tower exhaust gas concentration detecting instrument, two exhaust gas concentration detecting instruments to be connected by concentration signal line Controller, controller, which is connected by control line and controls every group, surmounts valve, or connects and control each sub- valve. Judge each self-operating, stopping or exchanging operation time by concentration determination.
Since absorption is to compare for a long time(Such as 11-24 hours)The processing procedure of accumulation, and it is the short time to desorb(Such as 1 hour or so)Several processing procedures.When the attached desorber of traditional double suction is an absorption, another is desorbed.Two Only carry out in turn, two equipment can not work asynchronously, one work when, another stop it is waiting for a long time, treatment effeciency is low.
Utility model works process:
When absorption, exhaust gas surmounts valve from first group(Or one only adsorbs sub- valve)Pass through first adsorption-desorption tower Exhaust gas entrance enter adsorption-desorption tower carry out adsorption operation, when second adsorb Analytic Tower regeneration ending when, open its mutually Lead to sub- valve and another adsorbs sub- valve and is carried out at the same time adsorption operation into second adsorption-desorption tower.
When desorption, stripping gas surmounts valve from second group(Or one only desorbs sub- valve)Pass through first adsorption-desorption The stripping gas entrance of tower enters adsorption-desorption tower and carries out desorption operation, at the end of the absorption that second adsorbs Analytic Tower, opens The sub- valve of its intercommunication and another desorb sub- valve and are carried out at the same time desorption operation into second adsorption-desorption tower.
The opening and closing for adsorbing and desorbing sub- valve are after being detected by respective exhaust gas concentration detecting instrument, by controlling Device judges opportunity, then go to control respectively by control line.
Controller controls first group of sub- valve of the absorption of surmount valve one and first works 1 hour or so, rear to open second It adsorbs sub- valve to work at the same time again 10-23 hours, is then switched off first absorption sub- valve 1 hour or so, second absorption Valve works on 1 hour or so;Then controller control, which lives another group of group and surmounts one of valve, desorbs sub- valve working 1 hour Left and right is closed, and opens second desorption sub- valve working 1 hour or so at this time.And close first desorb sub- valve while or After person closes 1 hour or so, first sub- valve of absorption starts subjob again, and so cycle carries out, and two adsorption-desorption towers are several There is no the off-air time, acquisition, which has, to be connected in parallel and have the dual ability to work being connected in series with.
Advantageous effect:
The each tower body of the utility model makes full use of, and reduces dead period.By the design of valve and pipeline, reach one When adsorption-desorption tower desorbs, the air inlet of the tower is automatically into another tower.When one adsorption-desorption tower absorption, the stripping gas gas of the tower Automatically into another tower.The utilization ratio of two towers improves by about one time than the treatment effeciency of traditional parallel double tower.And it is logical The test of over-richness switches, and high degree of automation reduces the error of manual intervention and reduces hand labor intensity.It is suitble to processing The big Work places of exhausted air quantity use.
Description of the drawings
Fig. 1 is a cross-sectional view of the utility model;
In figure, 1, air inlet pipe A;2- intake valves A(Adsorb sub- valve);3- air inlet cross over pipes;5- air inlets A;6- concentration is surveyed Measure instrument A;7- stripping gas entrances A;8- desorbs air valve A(Desorb sub- valve);9- stripping liquids export A;10 air inlet coupling cocks;11- into Tracheae B;12- intake valves B(Adsorb sub- valve);13- stripping gas cross over pipes;15- imports B;16- concentration measuring apparatus B;17- is desorbed Gas entrance B;18- desorbs air valve B(Desorb sub- valve);19- stripping liquids export B;20- stripping gas coupling cocks;21- desorbs tracheae A; 22- desorbs tracheae B;30- control devices;31- air inlet coupling cock control lines;32- intake valve A control lines;33- concentration signal lines A; 34- desorbs air valve control line;35- desorbs air valve A control lines;36- concentration signal lines B;37- stripping gas coupling cock control lines;38- Desorb air valve B control lines;100- adsorption tanks A;200- adsorption tanks B.
Specific implementation mode
As shown in Figure 1 surmounts valve adsorption-desorption device, has adsorption-desorption tower A and adsorption-desorption tower B, every absorption solution Inhaling tower has exhaust gas entrance, stripping gas entrance, or also waste liquid outlet.Another that there are two groups to surmount valve, every group surmounts valve tool Have three combination control sub- valves or similar to three valves control and make-break capacity.
One end outlet of first group of surmount valve two sub- valve of absorption respectively connected the useless of two adsorption-desorption towers Gas entrance, the other end outlet of this two sub- valves of absorption of both ends difference unicom of the sub- valve of another intercommunication;Second group surmounts One end outlet of two sub- valves of desorption of valve respectively connected the stripping gas entrance of two adsorption-desorption towers, another intercommunication The other end outlet of this two sub- valves of desorption of both ends difference unicom of sub- valve.
Also there is exhaust gas concentration detecting instrument, two exhaust gas concentration detecting instruments to be connected by concentration signal line in every tower Then controller, controller, which is connected by control line and controls every group, surmounts valve, or connects and control each sub- valve Door.

Claims (2)

1. one kind surmounting valve adsorption-desorption device, there is adsorption-desorption tower A and adsorption-desorption tower B, every adsorption-desorption tower to have Exhaust gas entrance, stripping gas entrance, or also waste liquid outlet, it is characterised in that:Another to surmount valve with two groups, every group surmounts valve Sub- valve with three combination control;
The exhaust gas that one end outlet of first group of two sub- valve of absorption for surmounting valve respectively connected two adsorption-desorption towers enters Mouthful, the other end outlet of this two sub- valves of absorption of both ends difference unicom of the sub- valve of another intercommunication;Second group surmounts valve One end outlets of two sub- valves of desorption respectively connected the stripping gas entrances of two adsorption-desorption towers, the sub- valve of another intercommunication The other end outlet of this two sub- valves of desorption of both ends difference unicom of door.
2. surmounting valve adsorption-desorption device as described in claim 1, it is characterised in that:Also there is exhaust gas concentration inspection in every tower Instrument is surveyed, two exhaust gas concentration detecting instruments are connected to controller by concentration signal line, and controller is connected by control line And control every group and surmount valve, or connect and control each sub- valve.
CN201721607735.6U 2017-11-28 2017-11-28 Surmount valve adsorption-desorption device Active CN207886908U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721607735.6U CN207886908U (en) 2017-11-28 2017-11-28 Surmount valve adsorption-desorption device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721607735.6U CN207886908U (en) 2017-11-28 2017-11-28 Surmount valve adsorption-desorption device

Publications (1)

Publication Number Publication Date
CN207886908U true CN207886908U (en) 2018-09-21

Family

ID=63548171

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721607735.6U Active CN207886908U (en) 2017-11-28 2017-11-28 Surmount valve adsorption-desorption device

Country Status (1)

Country Link
CN (1) CN207886908U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107824004A (en) * 2017-11-28 2018-03-23 上海亿景能源科技有限公司 Surmount valve adsorption-desorption combination unit

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107824004A (en) * 2017-11-28 2018-03-23 上海亿景能源科技有限公司 Surmount valve adsorption-desorption combination unit

Similar Documents

Publication Publication Date Title
CN201926252U (en) Mobile pipe drying device
CN201313030Y (en) Silica-gel dryer
CN104833689A (en) Online analyzer for enriching total mercury in flue gas based on dry process and analysis method
CN109358143A (en) A kind of water-eliminating method, sample injection method and its device for gas concentration sampling
CN207886908U (en) Surmount valve adsorption-desorption device
CN206535383U (en) A kind of compressed air drying adsorbent equipment
CN102928323B (en) Air purification filtering material testing experimental system
CN105214632A (en) The full-automatic desorption and regeneration device of charcoal absorption on-line monitoring for VOCs treatment
CN101093092A (en) Air conditioner
CN204065045U (en) Denitration demercuration catalyst activity assessment device
CN107824004A (en) Surmount valve adsorption-desorption combination unit
CN207238718U (en) A kind of laboratory open air exhaust control system
RU163643U1 (en) COMPRESSED AIR DRY UNIT
CN108871884A (en) A kind of natural gas automatic continuous sampling system of solar control
CN204556581U (en) For the carrier gas purification plant of Process Gas Chromatograph
CN204395752U (en) A kind of equipment for treating exhaust emission
CN207970627U (en) A kind of intelligent control filter device
CN204008237U (en) A kind of vacuum line system for gas sampling
CN208054913U (en) A kind of single column air separating type nitrogen gas generating system
CN206616012U (en) Medical oxygen producing purifying plant
CN211576862U (en) Activated carbon filling device for simulation experiment
CN207100367U (en) A kind of air-conditioned cold store removes machine with CO2
CN212440630U (en) Rubber device n-hexane tail gas adsorption recovery device
CN211577088U (en) Activated carbon regeneration testing arrangement for simulation experiment
CN205056035U (en) A full -automatic desorption regenerating unit of on -line monitoring for organic waste gas handles

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant