CN105817130A - Device for efficient treatment of exhaust gas hydrogen sulfide - Google Patents
Device for efficient treatment of exhaust gas hydrogen sulfide Download PDFInfo
- Publication number
- CN105817130A CN105817130A CN201610305127.3A CN201610305127A CN105817130A CN 105817130 A CN105817130 A CN 105817130A CN 201610305127 A CN201610305127 A CN 201610305127A CN 105817130 A CN105817130 A CN 105817130A
- Authority
- CN
- China
- Prior art keywords
- tank
- tourie
- storage tank
- sulfur foam
- solid
- 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.)
- Pending
Links
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 239000007789 gas Substances 0.000 title claims abstract description 22
- 229910000037 hydrogen sulfide Inorganic materials 0.000 title abstract description 14
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 58
- 229910052717 sulfur Inorganic materials 0.000 claims abstract description 52
- 239000011593 sulfur Substances 0.000 claims abstract description 52
- 239000006260 foam Substances 0.000 claims abstract description 35
- 239000007788 liquid Substances 0.000 claims abstract description 25
- 239000007791 liquid phase Substances 0.000 claims abstract description 4
- 239000007790 solid phase Substances 0.000 claims abstract description 4
- 230000001172 regenerating effect Effects 0.000 claims description 22
- 239000002912 waste gas Substances 0.000 claims description 20
- 239000005864 Sulphur Substances 0.000 claims description 8
- 239000012530 fluid Substances 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 6
- 241000628997 Flos Species 0.000 claims description 3
- 238000010521 absorption reaction Methods 0.000 abstract description 9
- 238000006477 desulfuration reaction Methods 0.000 abstract description 6
- 230000008929 regeneration Effects 0.000 abstract description 6
- 238000011069 regeneration method Methods 0.000 abstract description 6
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 230000008901 benefit Effects 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000000243 solution Substances 0.000 description 24
- 230000003009 desulfurizing effect Effects 0.000 description 12
- 239000003795 chemical substances by application Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 6
- 239000002131 composite material Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000008439 repair process Effects 0.000 description 4
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000009719 regenerative response Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 210000003169 central nervous system Anatomy 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 230000000622 irritating effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 208000020470 nervous system symptom Diseases 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000035943 smell Effects 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/52—Hydrogen sulfide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/96—Regeneration, reactivation or recycling of reactants
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The invention provides a device for efficient treatment of exhaust gas hydrogen sulfide. The device comprises an absorption tank, a regeneration tank, a sulfur foam storage tank and a solid-liquid separator which are sequentially connected, wherein desulfuration pregnant solution flowing out of the absorption tank enters the regeneration tank and returns to the absorption tank as circulating liquid through pipelines respectively, an ejector is arranged in the absorption tank, a solid-phase discharge outlet and a liquid-phase outlet connected with the sulfur foam storage tank are formed in the solid-liquid separator, a barren liquor circulating pump used for injecting barren liquor into the absorption tank is arranged on the sulfur foam storage tank, the regeneration tank is provided with an air exhaust port and an air pump used for sucking air into the regeneration tank, and a sulfur foam pump is arranged between the sulfur foam storage tank and the solid-liquid separator. The device has the advantages of being high in desulfuration efficiency, free of secondary pollution, small in size and sensitive in reaction, regenerable at normal temperature and pressure, convenient to manage, low in energy consumption, low in operation cost and the like. Especially, at normal pressure or negative pressure, it is guaranteed that exhaust gas can enter the device for hydrogen sulfide removal.
Description
Technical field
The present invention relates to chemical pollution treatment and purification equipment technical field, especially relate to a kind of efficiency of waste gas hydrogen sulphide disposal unit.
Background technology
Hydrogen sulfide is to have zest and asphyxiant colourless gas.Low concentration contact only has respiratory tract and the local irritant effect of eye, and during high concentration, general action is more apparent, shows as central nervous system symptom and symptom of suffocating.Hydrogen sulfide has " addled egg sample " abnormal smells from the patient, but high concentration quickly causes olfactory fatigue and unconsciously its taste.Containing hydrogen sulfide gas in gas water after waste gas and gas dehydration, if the most treated, evaporate in air, serious foul odour can be produced, cause air pollution, have a strong impact on the healthy of staff and surrounding resident.And undressed hydrogen sulfide gas, can produce huge corrosion to pipe-line equipment etc. on successive projects, work the mischief.At present, commonly used alkali absorption method and dry desulfurizing process, the waste liquid of generation, solid waste are difficult to process, environment are caused secondary pollution.Simultaneously for normal pressure waste gas, pressurized equipment need to be used, there is device volume big, the problems such as investment cost is high.
Summary of the invention
The present invention proposes a kind of efficiency of waste gas hydrogen sulphide disposal unit, and high-efficiency desulfurization, pollution abatement, investment cost is low simultaneously.
The technical scheme is that and be achieved in that:
A kind of efficiency of waste gas hydrogen sulphide disposal unit, including the tourie being sequentially connected with, regenerating tank, sulfur foam storage tank and solid-liquid separator；The sulfur removing pregnant solution that described tourie flows out respectively enters described regenerating tank by the road and returns tourie as circulation fluid；The ejector for from top to bottom being sprayed by waste gas it is provided with in described tourie；Described solid-liquid separator is provided with solid phase floss hole and the liquid-phase outlet being connected by pipeline with described sulfur foam storage tank；Described sulfur foam storage tank is provided with the lean solution circulating pump in order to lean solution to be injected into described tourie；Described regenerating tank is provided with air outlet and the air pump for air-breathing in regenerating tank；Sulfur foam pump it is provided with between described sulfur foam storage tank and described solid-liquid separator.
Further, described tourie is provided with liquidometer and Pressure gauge.
Further, it is provided with check valve between described lean solution circulating pump and described sulfur foam storage tank.
Further, it is designed with check valve between described tourie and described regenerating tank and between described regenerating tank and described sulfur foam storage tank and between described sulfur foam storage tank and described solid-liquid separator.
Further, the clean gas outlet of described tourie and the import of sulphur-containing exhaust gas are equipped with check valve.
Further, described ejector is arranged on the top of described tourie, its simultaneously with described sulphur-containing exhaust gas import and return the sulfur removing pregnant solution pipeline of tourie as circulation fluid and be connected.
Have employed technique scheme, the invention have the benefit that
Desulfuration efficiency height, non-secondary pollution, equipment volume is little, be quick on the draw, the advantages such as normal temperature and pressure is renewable, convenient management, energy consumption are low, operating cost is low.It is crucial that in the case of normal pressure or negative pressure, can guarantee that waste gas carries out removing the process of hydrogen sulfide in entering device.
Accompanying drawing explanation
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be briefly described below, apparently, accompanying drawing in describing below is only some embodiments of the present invention, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the system schematic of the present invention.
Wherein: 1-tourie；2-regenerating tank；3-sulfur foam storage tank；4-solid-liquid separator；5-liquidometer；6-air pump；7-lean solution circulating pump；8-sulfur foam pump；9-Pressure gauge；10-ejector.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is only a part of embodiment of the present invention rather than whole embodiments.Based on the embodiment in the present invention, the every other embodiment that those of ordinary skill in the art are obtained under not making creative work premise, broadly fall into the scope of protection of the invention.
A kind of efficiency of waste gas hydrogen sulphide disposal unit, as it is shown in figure 1, include tourie 1, regenerating tank 2, sulfur foam storage tank 3 and the solid-liquid separator 4 being sequentially connected with；The sulfur removing pregnant solution that described tourie 1 flows out respectively enters described regenerating tank 2 by the road and returns tourie 1 as circulation fluid；The ejector 10 for from top to bottom being sprayed by waste gas it is provided with in described tourie 1；Described solid-liquid separator 4 is provided with solid phase floss hole and the liquid-phase outlet being connected by pipeline with described sulfur foam storage tank；Described sulfur foam storage tank 3 is provided with the lean solution circulating pump 7 in order to lean solution to be injected into described tourie 1；Described regenerating tank 2 is provided with air outlet and the air pump 6 for air-breathing in regenerating tank；It is provided with sulfur foam pump 8 between described sulfur foam storage tank 3 and described solid-liquid separator 4.
Feature for exhaust gas pressure low (normal pressure or negative pressure), ejector is used to introduce exhaust gas in tourie, react with efficient composite desulfurizer in tourie, hydrogen sulfide in waste gas is all absorbed, the desulfurizing agent absorbing hydrogen sulfide enters regenerating tank and the air oxidation generation drusen blasted, desulfurizing agent after filtering enters back into tourie, completes the recycling of desulfurizing agent.Concrete course of reaction is as follows:
Absorb and react:
R-X (composite desulfurizing agent)+H2S→R-HS+HX
Regenerative response:
Composite desulfurizing agent system is reacted with hydrogen sulfide in tourie, forms firm sulfide, forms sulfur removing pregnant solution, and rich solution is sufficiently mixed with air in regenerating tank, rapid regeneration under the effect of composite catalyst, generates sulfur.Lean solution recycles.The Sulfur capacity of desulfurizing agent is high.The Sulfur capacity of this desulfurizing agent is up to 0.3%～0.5%；And the Sulfur capacity of the most on-the-spot general desulfurizing agent is less than 0.1%.Absorbing reaction to complete in 10 seconds, absorb response speed fast, not absorbing carbon dioxide, the impact that desulfurizing agent absorption reaction is produced by carbon dioxide can be ignored.Meanwhile, reproduction speed is fast.The complex catalyst system of exploitation makes sulfur removing pregnant solution reproduction speed very fast, and general only can completing in several seconds is reacted.
It should be noted that because absorbing and being all mainly chemical reaction with regenerative process, so absorption efficiency is high, reproduction speed is also fast, and will not be stripped off sulfide in regenerative process.Whole system is only because taking away a part of liquid in drusen separation process, so only existing the loss of fraction band liquid.In regenerative process, the drusen of generation is very big, and solid-liquid is easily isolated, and separating technology is fairly simple.In running outside sulphur removal sulphur, do not produce any refuse, thus dirty without secondary.
Being provided with liquidometer 5 and Pressure gauge 9 on described tourie, staff can observe the force value in tank and liquid level condition intuitively, such as emergency situations, can handle it in time.
It is pointed out that and be provided with check valve between described lean solution circulating pump 7 and described sulfur foam storage tank 3.It is designed with check valve between described tourie 1 and described regenerating tank 2 and between described regenerating tank 2 and described sulfur foam storage tank 3 and between described sulfur foam storage tank 3 and described solid-liquid separator 4, it is equipped with check valve on the described clean gas outlet of tourie 1 and the import of sulphur-containing exhaust gas, effectively prevents liquid from flowing backwards.
Wherein, described ejector 10 is arranged on the top of described tourie, its simultaneously with described sulphur-containing exhaust gas import and return the sulfur removing pregnant solution pipeline of tourie as circulation fluid and be connected.First in the case of normal pressure or negative pressure, injection apparatus is utilized to introduce exhaust gas into desulfuration absorbing tower, it is not necessary to pressurized equipment.
Waste gas initially enters the ejector of tourie 1 doctor solution with circulating pump through pipeline and is sufficiently mixed, and is ejected into bottom above tourie 1.In tourie 1, hydrogen sulfide gas is absorbed after being sufficiently mixed with doctor solution, purifies gas emptying, and doctor solution enters ejector 10 through a part of self-loopa liquid as absorption tower of circulating pump, and another part enters the air regenesis that regenerating tank is come with aerator.In regenerating tank, use air oxidation principle, utilize efficient composite catalyst, make desulfurizing agent rich solution at normal temperature and pressure oxidation regeneration.Sulfide in doctor solution is oxidized to sulfur, and desulfurizing agent rich solution is reproduced into lean solution.
Lean solution enters sulfur foam storage tank together with sulfur foam, and sulfur foam storage tank upper clear supernate is back to tourie 1, and bottom sulfur-bearing iodine solution enters solid-liquid separator 4 after sulfur foam pump pressurizes and separates the use of sulfur Posterior circle.Isolated sulfur stores.In running amount infused by sulfur number and regenerative process in the water yield taken away determine, need to run certain time is determined supplementing.
This device desulfuration efficiency height, non-secondary pollution, equipment volume is little, be quick on the draw, and normal temperature and pressure is renewable,.Under the conditions of ambient temperature 5～50 DEG C, absorb reaction the least with the efficiency change of regenerative response.The advantages such as convenient management, energy consumption are low, operating cost is low.It is crucial that in the case of normal pressure or negative pressure, can guarantee that waste gas carries out removing the process of hydrogen sulfide in entering device.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (6)
1. an efficiency of waste gas hydrogen sulphide disposal unit, it is characterised in that: include tourie, regenerating tank, sulfur foam storage tank and the solid-liquid separator being sequentially connected with；The sulfur removing pregnant solution that described tourie flows out respectively enters described regenerating tank by the road and returns tourie as circulation fluid；The ejector for from top to bottom being sprayed by waste gas it is provided with in described tourie；Described solid-liquid separator is provided with solid phase floss hole and the liquid-phase outlet being connected by pipeline with described sulfur foam storage tank；Described sulfur foam storage tank is provided with the lean solution circulating pump in order to lean solution to be injected into described tourie；Described regenerating tank is provided with air outlet and the air pump for air-breathing in regenerating tank；Sulfur foam pump it is provided with between described sulfur foam storage tank and described solid-liquid separator.
A kind of efficiency of waste gas hydrogen sulphide disposal unit the most according to claim 1, it is characterised in that: described tourie is provided with liquidometer and Pressure gauge.
A kind of efficiency of waste gas hydrogen sulphide disposal unit the most according to claim 1, it is characterised in that: it is provided with check valve between described lean solution circulating pump and described sulfur foam storage tank.
A kind of efficiency of waste gas hydrogen sulphide disposal unit the most according to claim 1, it is characterised in that: it is designed with check valve between described tourie and described regenerating tank and between described regenerating tank and described sulfur foam storage tank and between described sulfur foam storage tank and described solid-liquid separator.
A kind of efficiency of waste gas hydrogen sulphide disposal unit the most according to claim 1, it is characterised in that: it is equipped with check valve on the clean gas outlet of described tourie and the import of sulphur-containing exhaust gas.
A kind of efficiency of waste gas hydrogen sulphide disposal unit the most according to claim 1, it is characterised in that: described ejector is arranged on the top of described tourie, its simultaneously with described sulphur-containing exhaust gas import and return the sulfur removing pregnant solution pipeline of tourie as circulation fluid and be connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610305127.3A CN105817130A (en) | 2016-05-10 | 2016-05-10 | Device for efficient treatment of exhaust gas hydrogen sulfide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610305127.3A CN105817130A (en) | 2016-05-10 | 2016-05-10 | Device for efficient treatment of exhaust gas hydrogen sulfide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105817130A true CN105817130A (en) | 2016-08-03 |
Family
ID=56528497
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610305127.3A Pending CN105817130A (en) | 2016-05-10 | 2016-05-10 | Device for efficient treatment of exhaust gas hydrogen sulfide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105817130A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051190A (en) * | 2017-03-20 | 2017-08-18 | 浙江澳蓝环保科技有限公司 | A kind of wet desulphurization equipment of sulphur-containing exhaust gas |
| CN108421393A (en) * | 2018-04-28 | 2018-08-21 | 武汉国力通能源环保股份有限公司 | A kind of portable pipe container desulfurization safety device and its application method |
| TWI698272B (en) * | 2019-10-29 | 2020-07-11 | 漢科系統科技股份有限公司 | Exhaust gas treatment system |
| CN114797424A (en) * | 2022-04-18 | 2022-07-29 | 北京安星达环保技术发展有限公司 | Industrial organic waste gas absorption treatment or pretreatment device |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5210857A (en) * | 1975-07-16 | 1977-01-27 | Kimura Kakoki Kk | Process for removal of hydrogen sulfide |
| JPS59112824A (en) * | 1982-12-18 | 1984-06-29 | Sumitomo Heavy Ind Ltd | Wet removal of hydrogen sulfide |
| JPS61204024A (en) * | 1985-03-08 | 1986-09-10 | Mitsubishi Heavy Ind Ltd | Removing apparatus for hydrogen sulfide contained in gas |
| JPH01194930A (en) * | 1988-01-29 | 1989-08-04 | Dowa Mining Co Ltd | Removal of h2s in gas |
| CN102381688A (en) * | 2011-09-06 | 2012-03-21 | 武汉科技大学 | A method for preparing concentrated sulfuric acid by using H2S in artificial gas |
| CN102633235A (en) * | 2012-03-09 | 2012-08-15 | 江苏中显集团有限公司 | Method for preparing sodium sulfide by processing hydrogen sulfide acid gas and special device thereof |
| CN202751934U (en) * | 2012-08-08 | 2013-02-27 | 上海河图工程股份有限公司 | Sulfur tail gas absorption purification combination device with circulated absorbents |
| CN105238452A (en) * | 2015-09-08 | 2016-01-13 | 袁峥嵘 | System and method of removing high-concentration H2S from coal gas |
| CN205832931U (en) * | 2016-05-10 | 2016-12-28 | 四川西油致诚石油技术有限公司 | A kind of efficiency of waste gas hydrogen sulphide disposal unit |
-
2016
- 2016-05-10 CN CN201610305127.3A patent/CN105817130A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5210857A (en) * | 1975-07-16 | 1977-01-27 | Kimura Kakoki Kk | Process for removal of hydrogen sulfide |
| JPS59112824A (en) * | 1982-12-18 | 1984-06-29 | Sumitomo Heavy Ind Ltd | Wet removal of hydrogen sulfide |
| JPS61204024A (en) * | 1985-03-08 | 1986-09-10 | Mitsubishi Heavy Ind Ltd | Removing apparatus for hydrogen sulfide contained in gas |
| JPH01194930A (en) * | 1988-01-29 | 1989-08-04 | Dowa Mining Co Ltd | Removal of h2s in gas |
| CN102381688A (en) * | 2011-09-06 | 2012-03-21 | 武汉科技大学 | A method for preparing concentrated sulfuric acid by using H2S in artificial gas |
| CN102633235A (en) * | 2012-03-09 | 2012-08-15 | 江苏中显集团有限公司 | Method for preparing sodium sulfide by processing hydrogen sulfide acid gas and special device thereof |
| CN202751934U (en) * | 2012-08-08 | 2013-02-27 | 上海河图工程股份有限公司 | Sulfur tail gas absorption purification combination device with circulated absorbents |
| CN105238452A (en) * | 2015-09-08 | 2016-01-13 | 袁峥嵘 | System and method of removing high-concentration H2S from coal gas |
| CN205832931U (en) * | 2016-05-10 | 2016-12-28 | 四川西油致诚石油技术有限公司 | A kind of efficiency of waste gas hydrogen sulphide disposal unit |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051190A (en) * | 2017-03-20 | 2017-08-18 | 浙江澳蓝环保科技有限公司 | A kind of wet desulphurization equipment of sulphur-containing exhaust gas |
| CN108421393A (en) * | 2018-04-28 | 2018-08-21 | 武汉国力通能源环保股份有限公司 | A kind of portable pipe container desulfurization safety device and its application method |
| TWI698272B (en) * | 2019-10-29 | 2020-07-11 | 漢科系統科技股份有限公司 | Exhaust gas treatment system |
| CN114797424A (en) * | 2022-04-18 | 2022-07-29 | 北京安星达环保技术发展有限公司 | Industrial organic waste gas absorption treatment or pretreatment device |
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| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160803 |