CN206631409U - A kind of removing water environment, the equipment of compression ring border hydrogen sulfide - Google Patents
A kind of removing water environment, the equipment of compression ring border hydrogen sulfide Download PDFInfo
- Publication number
- CN206631409U CN206631409U CN201720267437.0U CN201720267437U CN206631409U CN 206631409 U CN206631409 U CN 206631409U CN 201720267437 U CN201720267437 U CN 201720267437U CN 206631409 U CN206631409 U CN 206631409U
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- CN
- China
- Prior art keywords
- reactor
- hydrogen sulfide
- desulfurizing agent
- water environment
- compression ring
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- 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
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- Gas Separation By Absorption (AREA)
- Treating Waste Gases (AREA)
Abstract
A kind of removing water environment, the equipment of compression ring border hydrogen sulfide, belong to removing hydrogen sulfide technical field, and reactor bottom is connected to spray thrower by circulator, and its bottom is equipped with desulfurizing agent, is fixedly arranged in the middle of filler；Desulfurizing agent is transported to spray thrower by circulator, and desulfurizing agent passes through filler, is recycled to reactor bottom；The H 2 S-containing gas being transferred in H 2 S-containing gas or water environment in compression ring border through distributor stripping in carrier gas, from reactor lateral leadin, H 2 S-containing gas is transferred in desulfurizing agent with desulfurizing agent adverse current upwardly through filler, hydrogen sulfide；Purified gas is transmitted back to compression ring border and recycled by drier and air-introduced machine successively from reactor head, or is transmitted back to water environment circulation blow-removing by distributor by air-introduced machine.Physical Absorption and chemical reaction are combined, H 2 S-containing gas and liquid removal agent adverse current are mobile, first pass through Physical Absorption and enter desulfurizing agent liquid phase, are chemically reacted in the liquid phase with desulfurization, so as to realize the removing of hydrogen sulfide.
Description
Technical field
The utility model belongs to removing hydrogen sulfide technical field, more particularly to a kind of removing water environment, compression ring border hydrogen sulfide
Equipment, for all kinds of sulfide hydrogen waste water, sulfide hydrogen waste gas removing hydrogen sulfide.
Background technology
Stripping is a kind of method for separating volatilizable composition in liquid phase.Absorption is a kind of side of selective absorbing gaseous substance
Method.Stripping stresses to stress for separating-purifying gaseous products for separating-purifying liquid-phase product, absorption.Stripping is mutually tied with absorbing
Close, using gas phase as carrier, realize the purpose for removing predetermined substance from water environment, compression ring border.
The content of the invention
The purpose of this utility model is to provide a kind of realization removing hydrogen sulfide for different separation purposes, different occasions,
Reduce water environment, the equipment of compression ring border concentration of hydrogen sulfide.
Remove water environment, the reaction principle of the equipment of compression ring border hydrogen sulfide：Physical Absorption and chemical reaction are combined, contained
Hydrogen sulfide gas and liquid removal agent adverse current are mobile, and hydrogen sulfide first passes through Physical Absorption and enters desulfurizing agent liquid phase, in the liquid phase with
Desulfurization chemically reacts, so as to realize the removing of hydrogen sulfide.
The technical solution of the utility model：
It is a kind of removing water environment, the equipment of compression ring border hydrogen sulfide, the equipment include spray thrower 3, circulator 4, reactor 5,
Drier 6, air-introduced machine 7 and distributor 8；
The described bottom of reactor 5 is connected to spray thrower 3 by circulator 4, and spray thrower 3 is located at the top of reactor 5；Desulfurization
Agent 1 is positioned over the bottom of reactor 5, and filler 2 is fixed on the middle part of reactor 5；Described desulfurizing agent 1 is transported to spray by circulator 4
Device 3, pass through filler 2 and be recycled to the bottom of reactor 5；
The described top of reactor 5 is connected by pipeline with the bottom of drier 6, and the top of drier 6 is connected with air-introduced machine 7,
Described air-introduced machine 7 is used to be expelled directly out from the purified gas of reactor 5；Or air-introduced machine 7 is connected with distributor 8, from reaction
The purified gas of device 5 is transmitted back to water environment circulation blow-removing by distributor 8；
The described bottom of reactor 5 is connected by pipeline with the top of distributor 8, the H 2 S-containing gas in compression ring border, or
The H 2 S-containing gas being transferred in water environment through the stripping of distributor 8 in carrier gas, from the lateral leadin of reactor 5, Containing Sulfur hydrogen
With the adverse current of desulfurizing agent 1 upwardly through filler 2, hydrogen sulfide is transferred in desulfurizing agent 1 body.
The beneficial effects of the utility model：
1st, it is to first pass through gas stripping by the vulcanization hydrogen migration in liquid phase during the depriving hydrogen sulphide processing of anaerobic reactor waste water
Into gas phase, then by hydrogen sulfide containing gas absorption cleaning, purified gas is as circulating carried.By controlling circulating carried
Tolerance and gas velocity, the concentration of hydrogen sulfide in anaerobic reactor is reduced to below the index of suitable anaerobe existence.
2nd, it is to first pass through gas stripping to turn the hydrogen sulfide in liquid phase during the depriving hydrogen sulphide processing of other sulfide hydrogen waste water
Move on in gas phase, then by hydrogen sulfide containing gas absorption cleaning, purified gas is as circulating carried.By controlling circulation to carry
The tolerance and gas velocity of gas, the concentration of water outlet hydrogen sulfide is reduced to the index of drainage requirement.
, H 2 S-containing gas depriving hydrogen sulphide processing when, be that hydrogen sulfide containing gas is transported into cleaning equipment to go desulfurization
Change hydrogen, after purified gas reaches the index of requirement, be transmitted back to original place and recycle or high altitude discharge.
Brief description of the drawings
Fig. 1 is a kind of removing water environment, the equipment structure chart of compression ring border hydrogen sulfide.
Embodiment
Below in conjunction with accompanying drawing and technical scheme, specific embodiment of the present utility model is further illustrated.
Embodiment
It is a kind of removing water environment, the equipment of compression ring border hydrogen sulfide, the equipment include spray thrower 3, circulator 4, reactor 5,
Drier 6, air-introduced machine 7 and distributor 8；
The described bottom of reactor 5 is connected to spray thrower 3 by circulator 4, and spray thrower 3 is located at the top of reactor 5；It is described
Desulfurizing agent 1 be positioned over the bottom of reactor 5, filler 2 is fixed on the middle part of reactor 5；Described desulfurizing agent 1 is conveyed by circulator 4
To spray thrower 3, pass through filler 2 and be recycled to the bottom of reactor 5；
The described top of reactor 5 is connected by pipeline with the bottom of drier 6, and the top of drier 6 is connected with air-introduced machine 7,
Described air-introduced machine 7 is used to be expelled directly out from the purified gas of reactor 5；Or air-introduced machine 7 is connected with distributor 8, from reaction
The purified gas of device 5 is transmitted back to water environment circulation blow-removing by distributor 8；
The described bottom of reactor 5 is connected by pipeline with the top of distributor 8, the H 2 S-containing gas in compression ring border, or
The H 2 S-containing gas being transferred in water environment through the stripping of distributor 8 in carrier gas, from the lateral leadin of reactor 5, Containing Sulfur hydrogen
With the adverse current of desulfurizing agent 1 upwardly through filler 2, hydrogen sulfide is transferred in desulfurizing agent 1 body.
Made of pvc material in 0.4 meter × 3 meters of φ column type reactor, 500 liters of desulfurizing agent is filled, middle part is filled out
2 meters of high fillers are filled, continuous circulator circulation desulfurization agent, wine guide circulating carried are set.In the meter per second of empty tower gas velocity 0.6, spray
8 cubic metres of density/（Square metre * hours）, under conditions of 4 liters/m of liquid-gas ratio liquid-gas ratio, in anaerobic reactor liquid phase
Hydrogen sulfide carries out stripping, absorbing and removing., can be by the vulcanization of anaerobic reactor liquid phase under conditions of 1 meter of distributor submergence
Hydrogen concentration is reduced to below the index of the existence of suitable anaerobe.
Claims (1)
1. a kind of removing water environment, the equipment of compression ring border hydrogen sulfide, it is characterised in that the equipment includes spray thrower (3), circulator
(4), reactor (5), drier (6), air-introduced machine (7) and distributor (8)；
Described reactor (5) bottom is connected to spray thrower (3) by circulator (4), and spray thrower (3) is located at reactor (5) top
Portion；Desulfurizing agent (1) is positioned over reactor (5) bottom, and filler (2) is fixed in the middle part of reactor (5)；Described desulfurizing agent (1) by
Circulator (4) is transported to spray thrower (3), passes through filler (2) and is recycled to reactor (5) bottom；
It is connected at the top of described reactor (5) by pipeline with drier (6) bottom, at the top of drier (6) with air-introduced machine (7) even
Connect, described air-introduced machine (7) is used to be expelled directly out from reactor (5) purified gas；Or air-introduced machine (7) and distributor (8)
It is connected, water environment circulation blow-removing is transmitted back to from reactor (5) purified gas by distributor (8)；
Described reactor (5) bottom is connected by pipeline with distributor (8) top, the H 2 S-containing gas in compression ring border, or
The H 2 S-containing gas being transferred in water environment through distributor (8) stripping in carrier gas, from reactor (5) lateral leadin, Containing Sulfur
With desulfurizing agent (1) countercurrently upwardly through filler (2), hydrogen sulfide is transferred in desulfurizing agent (1) hydrogen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720267437.0U CN206631409U (en) | 2017-03-17 | 2017-03-17 | A kind of removing water environment, the equipment of compression ring border hydrogen sulfide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720267437.0U CN206631409U (en) | 2017-03-17 | 2017-03-17 | A kind of removing water environment, the equipment of compression ring border hydrogen sulfide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206631409U true CN206631409U (en) | 2017-11-14 |
Family
ID=60249796
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720267437.0U Expired - Fee Related CN206631409U (en) | 2017-03-17 | 2017-03-17 | A kind of removing water environment, the equipment of compression ring border hydrogen sulfide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206631409U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113247982A (en) * | 2021-06-07 | 2021-08-13 | 赛恩斯环保股份有限公司 | High-sulfur wastewater recycling treatment method and system |
-
2017
- 2017-03-17 CN CN201720267437.0U patent/CN206631409U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113247982A (en) * | 2021-06-07 | 2021-08-13 | 赛恩斯环保股份有限公司 | High-sulfur wastewater recycling treatment method and system |
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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: 20171114 Termination date: 20200317 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |