JPH09234334A - Hydrogen sulfide desulfurization apparatus and desulfurization of hydrogen sulfide-containing gas - Google Patents
Hydrogen sulfide desulfurization apparatus and desulfurization of hydrogen sulfide-containing gasInfo
- Publication number
- JPH09234334A JPH09234334A JP8045739A JP4573996A JPH09234334A JP H09234334 A JPH09234334 A JP H09234334A JP 8045739 A JP8045739 A JP 8045739A JP 4573996 A JP4573996 A JP 4573996A JP H09234334 A JPH09234334 A JP H09234334A
- Authority
- JP
- Japan
- Prior art keywords
- desulfurization
- hydrogen sulfide
- treatment tank
- yeast extract
- sulfuric acid
- 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
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Treating Waste Gases (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は微生物を利用した硫
化水素の脱硫装置及びそれを用いた硫化水素含有ガスの
脱硫方法に関し、特に地熱発電プラントで発生する硫化
水素含有ガスの脱硫に好適な脱硫装置及びそれを用いた
脱硫方法に関する。TECHNICAL FIELD The present invention relates to a desulfurization apparatus for hydrogen sulfide using microorganisms and a desulfurization method for hydrogen sulfide-containing gas using the same, and particularly to desulfurization suitable for desulfurization of hydrogen sulfide-containing gas generated in a geothermal power plant. The present invention relates to an apparatus and a desulfurization method using the apparatus.
【0002】[0002]
【従来の技術】地熱発電プラントにおいては高濃度の硫
化水素を含むガスが発生する。この硫化水素含有ガスの
処理方法の一つとして、地熱発電プラントで発生する硫
化水素含有ガスを高温・好酸硫黄酸化微生物を用いた微
生物処理槽に導いて脱硫処理し、脱硫に伴い生成する硫
酸によって酸性化した微生物処理槽の培養液を還元井に
戻す熱水に添加することによって効率のよい脱硫処理を
行うことができ、しかも還元井に戻す熱水のpHが高く
なることにより還元井の閉塞が防止できる、微生物を利
用した脱硫方法がある。2. Description of the Related Art A gas containing a high concentration of hydrogen sulfide is generated in a geothermal power plant. As one of the methods for treating the hydrogen sulfide-containing gas, the hydrogen sulfide-containing gas generated in a geothermal power plant is introduced into a microbial treatment tank using a high-temperature / sulfur-acid-oxidizing microorganism for desulfurization treatment, and the sulfuric acid generated by the desulfurization is generated. Efficient desulfurization can be performed by adding the culture solution of the microbial treatment tank that has been acidified by the hot water returned to the reduction well, and the pH of the hot water returned to the reduction well increases There is a desulfurization method using microorganisms that can prevent clogging.
【0003】前記脱硫方法の概略を図2を用いて説明す
る。地熱発電所(図示無し)では高濃度硫化水素含有不
凝縮ガス1は内部に硫黄酸化微生物を含む脱硫液2(温
度70℃、pH2.5、硫酸酸性)が充填された気泡塔
型の微生物処理槽3に空気あるいは酸素4とともに導か
れる。高濃度硫化水素含有不凝縮ガス1は、ガス中の硫
化水素が微生物処理槽3で酸化され低濃度硫化水素含有
不凝縮ガス5となり大気に放散される。微生物処理槽3
中の微生物には Sulfolobus 属の一種が用いられる。微
生物処理槽3の脱硫液2のpHは硫化水素が酸化され硫
黄を含む酸に転換されるに伴い経時的に低下する。硫酸
生成に伴い酸性化した脱硫液2は微生物処理槽3から菌
体分離フィルタ6を通じて酸性水7として抜き出される
と同時に、濃縮菌体8は微生物処理槽3に戻される。こ
のようにして得られた酸性水7が還元井(図示無し)に
注入されることにより熱水のpHが低下し、スケール付
着による還元井の閉塞が軽減される。一方、抜き出され
た酸性水7と同量の新しい脱硫液9が脱硫液タンク10
から、増殖用培養槽14で増殖した菌体16とも菌体供
給ポンプ15によって、微生物処理槽3に導入され連続
的に脱硫が行われる。菌体分離フィルタ6による回収及
び増殖用培養槽14からの菌体投入により菌体の量は微
生物処理槽3の中で一定以上に保たれる。The outline of the desulfurization method will be described with reference to FIG. At a geothermal power plant (not shown), a high-concentration hydrogen sulfide-containing non-condensing gas 1 is filled with a desulfurization liquid 2 (temperature 70 ° C., pH 2.5, sulfuric acid acidity) containing sulfur-oxidizing microorganisms, which is a bubble column type microbial treatment. It is introduced into the tank 3 together with air or oxygen 4. In the high-concentration hydrogen sulfide-containing non-condensable gas 1, hydrogen sulfide in the gas is oxidized in the microbial treatment tank 3 to become a low-concentration hydrogen sulfide-containing non-condensed gas 5, which is released to the atmosphere. Microbial treatment tank 3
One of the genus Sulfolobus is used as the microorganism. The pH of the desulfurization liquid 2 in the microorganism treatment tank 3 decreases with time as hydrogen sulfide is oxidized and converted into an acid containing sulfur. The desulfurization liquid 2 that has been acidified with the production of sulfuric acid is extracted from the microbial treatment tank 3 as acidic water 7 through the microbial cell separation filter 6, and at the same time, the concentrated microbial cells 8 are returned to the microbial treatment tank 3. The acidic water 7 thus obtained is injected into a reduction well (not shown), whereby the pH of the hot water is lowered and clogging of the reduction well due to scale adhesion is reduced. On the other hand, a new desulfurization liquid 9 in the same amount as the extracted acidic water 7 is desulfurization liquid tank 10.
From the above, both the bacterial cells 16 grown in the growth culture tank 14 are introduced into the microorganism treatment tank 3 by the bacterial cell supply pump 15, and desulfurization is continuously performed. The amount of microbial cells is kept above a certain level in the microbial treatment tank 3 by the collection by the microbial cell separation filter 6 and the introduction of the microbial cells from the growth culture tank 14.
【0004】[0004]
【発明が解決しようとする課題】前記方法において使用
される高温・好酸硫黄酸化微生物の増殖方法としては次
の二とおりの方法がある。その一つは、図2のように別
途設けられた増殖槽で、有機物を利用して増殖する従属
栄養槽増殖であり、もう一つは微生物処理槽で起こる硫
化水素酸化による独立栄養増殖である。前記の従来の技
術では微生物処理槽での増殖量が脱硫液による希釈量よ
り少なく、脱硫液の希釈による菌体減少のため経時的に
脱硫率が低下してしまう。そのため、菌体補充のための
増殖槽が必要であり、菌体増殖槽からの増殖液供給のた
めのコストが問題となっていた。There are the following two methods for growing high-temperature, sulfurous acid-oxidizing microorganisms used in the above method. One is heterotrophic growth, which is a separate growth tank as shown in FIG. 2, which grows by utilizing organic matter, and the other is autotrophic growth by hydrogen sulfide oxidation that occurs in the microorganism treatment tank. . In the above-mentioned conventional technique, the amount of growth in the microbial treatment tank is smaller than the amount diluted with the desulfurization liquid, and the desulfurization liquid is diluted, so that the bacterial cells are reduced and the desulfurization rate decreases with time. Therefore, a growth tank for supplementing the bacterial cells is required, and the cost for supplying the growth liquid from the bacterial cell growth tank has been a problem.
【0005】本発明は前記従来技術における問題点を解
決し、微生物処理槽での高温・好酸硫黄酸化微生物の増
殖を促進することができ、菌体補充のための増殖工程を
必要としない硫化水素脱硫装置及びそれを用いた脱硫方
法を提供することを目的とする。The present invention solves the above-mentioned problems in the prior art, can promote the growth of high-temperature / acid-acid sulfur-oxidizing microorganisms in a microorganism treatment tank, and does not require a growth step for supplementing the cells. An object is to provide a hydrodesulfurization apparatus and a desulfurization method using the same.
【0006】[0006]
【課題を解決するための手段】本発明は、(1)高温・
好酸硫黄酸化微生物を含む脱硫液を充填した微生物処理
槽と菌体回収フィルタとを備え、該微生物処理槽に硫化
水素含有ガスを通して硫化水素を硫酸に変換することに
より脱硫し、硫化水素濃度の低減した排ガスを排出する
とともに、硫酸を含んだ溶液を抜き出し、同量の脱硫液
を補充することにより連続的に脱硫を行う装置におい
て、微生物処理槽に補充する脱硫液に酵母エキスを連続
的に添加するポンプ及び酵母エキスタンクを設けてなる
ことを特徴とする硫化水素脱硫装置、及び(2)高温・
好酸硫黄酸化微生物を含む脱硫液を充填した微生物処理
槽と菌体回収フィルタとを備えた脱硫装置に、硫化水素
含有ガスを通して高温・好酸硫黄酸化微生物の作用によ
り硫化水素を硫酸に変換することによって脱硫し、硫化
水素濃度の低減した排ガスを排出するとともに、硫酸を
含んだ溶液を抜き出し、同量の脱硫液を補充することに
より連続的に脱硫を行う脱硫方法において、微生物処理
槽に補充する脱硫液に酵母エキスを連続的に添加し、前
記微生物処理槽における脱硫を酵母エキスの存在下に行
うことを特徴とする硫化水素含有ガスの脱硫方法であ
る。The present invention includes (1) high temperature
A microbial treatment tank filled with a desulfurization liquid containing a sulphate-oxidizing microorganism and a microbial cell recovery filter are provided, and desulfurization is performed by converting hydrogen sulfide to sulfuric acid by passing a hydrogen sulfide-containing gas through the microbial treatment tank to obtain a concentration of hydrogen sulfide. In a device that performs desulfurization continuously by discharging reduced exhaust gas, extracting a solution containing sulfuric acid, and replenishing the same amount of desulfurization liquid, yeast extract is continuously added to the desulfurization liquid to be added to the microbial treatment tank. A hydrogen sulfide desulfurization device characterized by comprising a pump for addition and a yeast extract tank, and (2) high temperature
Hydrogen sulfide-containing gas is passed through a desulfurization device equipped with a microbial treatment tank filled with a desulfurization liquid containing sulfur-acid-oxidizing microorganisms and a cell recovery filter, and hydrogen sulfide is converted to sulfuric acid by the action of high-temperature sulfur-oxidizing microorganisms oxidizing sulfur. In this desulfurization method, in which desulfurization is performed, exhaust gas with reduced hydrogen sulfide concentration is discharged, and a solution containing sulfuric acid is extracted and the same amount of desulfurization solution is replenished to continuously desulfurize the microbial treatment tank. Yeast extract is continuously added to the desulfurizing solution, and desulfurization is performed in the microorganism treatment tank in the presence of the yeast extract.
【0007】前記(2)の脱硫方法における脱硫液に添
加する酵母エキスの添加量は、脱硫液に対して0.00
01%以上とするのが好ましい。The amount of yeast extract added to the desulfurization solution in the desulfurization method of the above (2) is 0.00 relative to the desulfurization solution.
It is preferably set to 01% or more.
【0008】[0008]
【発明の実施の形態】酵母エキスの添加により、微生物
処理槽での酸転換率が上がり、高効率な硫酸生成が可能
となる。高温・好酸硫黄酸化微生物の増殖は硫酸生成と
連動しているため、これにより微生物処理槽での増殖量
が脱硫液の希釈量より大きくなり、脱硫処理に必要な菌
濃度が維持可能となる。BEST MODE FOR CARRYING OUT THE INVENTION The addition of yeast extract increases the acid conversion rate in the microbial treatment tank and enables highly efficient sulfuric acid production. Since the growth of high-temperature / acid-sulfuric acid-oxidizing microorganisms is linked to the production of sulfuric acid, the growth amount in the microbial treatment tank becomes larger than the dilution amount of the desulfurization solution, and the bacterial concentration required for desulfurization treatment can be maintained. .
【0009】以下、図面を参照して本発明を説明する。
図1は本発明の装置の1実施態様を示す概略フロー図で
ある。図1において、地熱発電所(図示せず)で発生し
た高濃度硫化水素含有不凝縮ガス1(通常1〜2%の硫
化水素を含む)は高温・好酸硫黄酸化微生物を含む脱硫
液2が充填された気泡塔型の微生物脱硫槽3に空気ある
いは酸素4とともに導かれる。脱硫液2は温度50〜9
0℃、好ましくは60〜80℃で、pH3以下、好まし
くは1〜2.5の硫酸酸性であり、適量の高温・好酸硫
黄酸化微生物を含んでおり、酵母エキスタンク11から
酵母エキス13が添加されて微生物脱硫槽3に供給され
る。The present invention will be described below with reference to the drawings.
FIG. 1 is a schematic flow chart showing one embodiment of the apparatus of the present invention. In FIG. 1, a high-concentration hydrogen sulfide-containing non-condensing gas 1 (usually containing 1 to 2% hydrogen sulfide) generated in a geothermal power plant (not shown) is a desulfurization liquid 2 containing a high temperature sulfur oxyacid-oxidizing microorganism. It is introduced together with air or oxygen 4 into the filled bubble column type microbial desulfurization tank 3. The desulfurization liquid 2 has a temperature of 50 to 9
At 0 ° C., preferably 60 to 80 ° C., pH 3 or less, preferably 1 to 2.5, sulfuric acid acidity, and an appropriate amount of high temperature / acid-acid sulfur-oxidizing microorganisms are contained, and yeast extract tank 11 to yeast extract 13 It is added and supplied to the microbial desulfurization tank 3.
【0010】高硫化水素含有不凝縮ガス1は、ガス中の
硫化水素が微生物処理槽3で高温・好酸硫黄酸化微生物
の作用により酸化されて硫酸として除かれ、低濃度硫化
水素含有不凝縮ガス5となり、大気に放散される。微生
物脱硫槽3中の高温・好酸硫黄酸化微生物は50〜90
℃の高温度、pH3以下の酸性域で硫化水素や硫黄を酸
化し、最終的に硫酸を生成する微生物である。この微生
物の好ましい例としてはスルフォロブス( Sulfolobus
)属の微生物があげられる。The high-concentration hydrogen sulfide-containing non-condensable gas 1 is a low-concentration hydrogen sulfide-containing non-condensing gas in which the hydrogen sulfide in the gas is oxidized in the microbial treatment tank 3 by the action of the high temperature sulfur oxyacid-oxidizing microorganisms and removed as sulfuric acid. It becomes 5 and is released to the atmosphere. 50 to 90 for high temperature and sulphate-oxidizing microorganisms in the microbial desulfurization tank 3.
It is a microorganism that oxidizes hydrogen sulfide and sulfur in an acidic range of pH 3 or less at a high temperature of ℃ and finally produces sulfuric acid. A preferred example of this microorganism is Sulfolobus.
) Microorganisms of the genus.
【0011】微生物処理槽3の脱硫液2のpHは硫化水
素が酸化され硫黄を含む酸(硫酸)に転換されるに伴い
経時的に低下する。硫酸生成に伴い酸性化した脱硫液2
は微生物処理槽3から菌体分離フィルタ6を通じて酸性
水7として抜き出されると同時に、菌体8は微生物処理
槽3に戻される。このようにして抜き出された酸性水7
が還元井(図示せず)に注入されることにより熱水のp
Hが低下し、スケール付着による還元井の閉塞が軽減さ
れる。The pH of the desulfurization liquid 2 in the microorganism treatment tank 3 decreases with time as hydrogen sulfide is oxidized and converted into an acid (sulfuric acid) containing sulfur. Desulfurization liquor acidified with sulfuric acid production 2
Is extracted from the microbial treatment tank 3 through the microbial cell separation filter 6 as acidic water 7, and at the same time, the microbial cells 8 are returned to the microbial treatment tank 3. Acidic water 7 extracted in this way
Is injected into the reduction well (not shown),
H is lowered, and blockage of the reduction well due to scale adhesion is reduced.
【0012】一方、抜き出された酸性水7と同量の新し
い脱硫液9が脱硫液タンク10から、微生物処理槽3に
導入される。それと同時に酵母エキスタンク11から酵
母エキスポンプ12により酵母エキス13が微生物処理
槽3に脱硫液の0.0001%となるよう添加される。
酵母エキスは微生物が活動するための必須アミノ酸(メ
チオニンなど)やビタミンの供給源となるものであり、
具体的にはディフコ社のバクト酵母抽出物(Difco
社:Bacto Yeast Extract)などが
使用できる。酵母エキスの添加により微生物処理槽3内
で高温・好酸硫黄酸化微生物が高効率で独立栄養増殖が
可能となり、フィルタ6による回収及び微生物処理槽3
中での高効率な増殖により菌体の量は微生物処理槽3の
中で一定以上に保たれる。その結果、高効率で連続的に
脱硫処理を行うことが可能となる。On the other hand, the same amount of fresh desulfurization liquid 9 as the extracted acidic water 7 is introduced into the microorganism treatment tank 3 from the desulfurization liquid tank 10. At the same time, the yeast extract 13 is added from the yeast extract tank 11 to the microbial treatment tank 3 by the yeast extract pump 12 so as to be 0.0001% of the desulfurization solution.
Yeast extract is a source of essential amino acids (such as methionine) and vitamins for the activity of microorganisms,
Specifically, Difco's Bacto yeast extract (Difco
Company: Bacto Yeast Extract) and the like can be used. By adding the yeast extract, the high temperature / sulfurous acid-oxidizing microorganisms in the microorganism treatment tank 3 can be propagated with high efficiency by autotrophic growth, and the recovery by the filter 6 and the microorganism treatment tank 3 can be performed.
Due to the highly efficient growth therein, the amount of bacterial cells is kept above a certain level in the microorganism treatment tank 3. As a result, it becomes possible to perform desulfurization treatment continuously with high efficiency.
【0013】微生物処理槽3中の菌体濃度は1×109
cells/ミリリットル以上、好ましくは2×109
cells/ミリリットル程度とする。The microbial cell concentration in the microorganism treatment tank 3 is 1 × 10 9
cells / ml or more, preferably 2 × 10 9
It is about cells / milliliter.
【0014】[0014]
【実施例】以下、実施例により酵母エキス添加の効果を
説明する。表1に示す条件で、微生物処理槽中の酵母エ
キス濃度を変化させて硫化水素の酸転換試験を行った。
結果は図3に示すとおりで、酵母エキス濃度が0.00
01%未満になると酸転換率が小さくなる。すなわち硫
酸生成量が小さくなるため十分な増殖ができない。よっ
て酵母エキス濃度は0.0001%以上必要である。[Examples] The effects of adding yeast extract will be described below with reference to Examples. Under the conditions shown in Table 1, an acid conversion test of hydrogen sulfide was conducted by changing the yeast extract concentration in the microorganism treatment tank.
The results are shown in Fig. 3, where the yeast extract concentration was 0.00
When it is less than 01%, the acid conversion rate becomes small. That is, the amount of sulfuric acid produced is small, so that sufficient growth cannot be achieved. Therefore, the yeast extract concentration needs to be 0.0001% or more.
【0015】[0015]
【表1】 [Table 1]
【0016】[0016]
【表2】 [Table 2]
【0017】[0017]
【発明の効果】微生物処理槽に酵母エキスを添加するこ
とにより微生物処理槽内で高温・好酸硫黄酸化微生物が
高効率で独立栄養増殖が可能となり、菌体濃度を必要濃
度以上に保つことができる。そのため、増殖用培養槽か
らの菌体の補充なしに連続的に酸性水製造(脱硫処理)
が可能となる。これによって増殖用培養槽からの菌体供
給が必要なくなり、菌体増殖液のコストが削減される。[Effects of the Invention] By adding yeast extract to the microorganism treatment tank, it becomes possible to highly efficiently autotrophically grow high-temperature, sulfurous acid-oxidizing microorganisms in the microorganism treatment tank, and to keep the bacterial cell concentration above the required concentration. it can. Therefore, continuous production of acidic water (desulfurization treatment) without supplementation of bacterial cells from the culture tank for growth
Becomes possible. As a result, it is not necessary to supply the bacterial cells from the culture tank for growth, and the cost of the bacterial cell growth liquid is reduced.
【図1】本発明の実施例に係る地熱発電所バイオ脱硫装
置のフロー図。FIG. 1 is a flow chart of a biodesulfurization device for a geothermal power plant according to an embodiment of the present invention.
【図2】従来の地熱発電所バイオ脱硫装置のフロー図。FIG. 2 is a flow diagram of a conventional geothermal power plant biodesulfurization apparatus.
【図3】酵母エキス濃度と酸転換率の関係を示す図。FIG. 3 is a graph showing the relationship between yeast extract concentration and acid conversion rate.
Claims (3)
を充填した微生物処理槽と菌体回収フィルタとを備え、
該微生物処理槽に硫化水素含有ガスを通して硫化水素を
硫酸に変換することにより脱硫し、硫化水素濃度の低減
した排ガスを排出するとともに、硫酸を含んだ溶液を抜
き出し、同量の脱硫液を補充することにより連続的に脱
硫を行う装置において、微生物処理槽に補充する脱硫液
に酵母エキスを連続的に添加するポンプ及び酵母エキス
タンクを設けてなることを特徴とする硫化水素脱硫装
置。1. A microbial treatment tank filled with a desulfurization liquid containing a high temperature sulfurous acid-oxidizing microorganism and a microbial cell recovery filter,
Desulfurization is performed by converting hydrogen sulfide into sulfuric acid by passing a hydrogen sulfide-containing gas through the microorganism treatment tank to discharge exhaust gas having a reduced hydrogen sulfide concentration, and a solution containing sulfuric acid is extracted and the same amount of desulfurization liquid is replenished. Thus, in a device for continuously desulfurizing, a hydrogen sulfide desulfurization device comprising a pump and a yeast extract tank for continuously adding a yeast extract to a desulfurization liquid to be replenished in a microorganism treatment tank.
を充填した微生物処理槽と菌体回収フィルタとを備えた
脱硫装置に、硫化水素含有ガスを通して高温・好酸硫黄
酸化微生物の作用により硫化水素を硫酸に変換すること
によって脱硫し、硫化水素濃度の低減した排ガスを排出
するとともに、硫酸を含んだ溶液を抜き出し、同量の脱
硫液を補充することにより連続的に脱硫を行う脱硫方法
において、微生物処理槽に補充する脱硫液に酵母エキス
を連続的に添加し、前記微生物処理槽における脱硫を酵
母エキスの存在下に行うことを特徴とする硫化水素含有
ガスの脱硫方法。2. A desulfurization apparatus equipped with a microbial treatment tank filled with a desulfurization liquid containing a high-temperature / sulfur-acid-acid-oxidizing microorganism and a microbial cell recovery filter is passed through a gas containing hydrogen sulfide to cause the action of the high-temperature / sulfur-acid-oxidizing microorganism. A desulfurization method in which desulfurization is performed by converting hydrogen sulfide to sulfuric acid, exhaust gas with reduced hydrogen sulfide concentration is discharged, and a solution containing sulfuric acid is extracted, and desulfurization liquid of the same amount is replenished for continuous desulfurization. In the method for desulfurization of hydrogen sulfide-containing gas, yeast extract is continuously added to a desulfurization liquid to be replenished in the microorganism treatment tank, and desulfurization in the microorganism treatment tank is performed in the presence of the yeast extract.
量が脱硫液に対して0.0001%以上であることを特
徴とする請求項2に記載の硫化水素含有ガスの脱硫方
法。3. The method for desulfurizing a hydrogen sulfide-containing gas according to claim 2, wherein the amount of yeast extract added to the desulfurization solution is 0.0001% or more based on the desulfurization solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8045739A JPH09234334A (en) | 1996-03-04 | 1996-03-04 | Hydrogen sulfide desulfurization apparatus and desulfurization of hydrogen sulfide-containing gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8045739A JPH09234334A (en) | 1996-03-04 | 1996-03-04 | Hydrogen sulfide desulfurization apparatus and desulfurization of hydrogen sulfide-containing gas |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09234334A true JPH09234334A (en) | 1997-09-09 |
Family
ID=12727695
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8045739A Pending JPH09234334A (en) | 1996-03-04 | 1996-03-04 | Hydrogen sulfide desulfurization apparatus and desulfurization of hydrogen sulfide-containing gas |
Country Status (1)
Country | Link |
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JP (1) | JPH09234334A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106434515A (en) * | 2016-09-12 | 2017-02-22 | 北京实力伟业环保科技有限公司 | Method for domesticating bacteria strains applied to biochemical treatment of sulfur-containing waste gas in viscose fiber industry |
-
1996
- 1996-03-04 JP JP8045739A patent/JPH09234334A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106434515A (en) * | 2016-09-12 | 2017-02-22 | 北京实力伟业环保科技有限公司 | Method for domesticating bacteria strains applied to biochemical treatment of sulfur-containing waste gas in viscose fiber industry |
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