CN106635210A - Method for removing hydrogen sulfide in biogas by using Acidithiobacillus caldus - Google Patents
Method for removing hydrogen sulfide in biogas by using Acidithiobacillus caldus Download PDFInfo
- Publication number
- CN106635210A CN106635210A CN201611010804.5A CN201611010804A CN106635210A CN 106635210 A CN106635210 A CN 106635210A CN 201611010804 A CN201611010804 A CN 201611010804A CN 106635210 A CN106635210 A CN 106635210A
- Authority
- CN
- China
- Prior art keywords
- biogas
- mesophilic
- hydrogen sulfide
- acidophilic
- thiobacillus
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
- C10L3/101—Removal of contaminants
- C10L3/102—Removal of contaminants of acid contaminants
- C10L3/103—Sulfur containing contaminants
-
- 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
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/84—Biological processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2866—Particular arrangements for anaerobic reactors
- C02F3/2893—Particular arrangements for anaerobic reactors with biogas recycling
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/20—Bacteria; Culture media therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/05—Biogas
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/32—Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
- C02F2103/325—Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters from processes relating to the production of wine products
-
- 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
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/59—Biological synthesis; Biological purification
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Microbiology (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Biomedical Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Biodiversity & Conservation Biology (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Zoology (AREA)
- Biotechnology (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Molecular Biology (AREA)
- Virology (AREA)
- Tropical Medicine & Parasitology (AREA)
- Medicinal Chemistry (AREA)
- Sustainable Development (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
本发明公开了一种喜温嗜酸硫杆菌去除沼气中硫化氢的方法,将待处理的沼气通入喜温嗜酸硫杆菌的发酵液中,通过喜温嗜酸硫杆菌的发酵去除沼气中的硫化氢,发酵温度为40~45℃。所述喜温嗜酸硫杆菌为中国微生物菌种保藏中心保藏的菌种编号为1.7296的菌株。喜温嗜酸硫杆菌的发酵液中菌体活细胞数为2.0×106个/mL~10.0×106个/mL。本方法具有操作方便,工艺流程简单,提高资源利用价值,节省费用、提高脱硫效率等优点,可以稳定高效地脱除沼气中的硫化氢,将有助于提高沼气利用水平,突破沼气脱硫难题。
The invention discloses a method for removing hydrogen sulfide in biogas by mesophilic acidophilic thiobacillus. hydrogen sulfide, the fermentation temperature is 40~45℃. The mesophilic acidophilic Thiobacillus is a strain with a strain number of 1.7296 preserved in the China Microorganism Culture Collection Center. The number of viable cells in the fermentation broth of mesophilic acidophilus thiobacterium was 2.0×10 6 cells/mL~10.0×10 6 cells/mL. The method has the advantages of convenient operation, simple process flow, improved resource utilization value, cost saving, and improved desulfurization efficiency, and can stably and efficiently remove hydrogen sulfide in biogas, which will help improve the utilization level of biogas and break through the difficult problem of biogas desulfurization.
Description
技术领域technical field
本发明属于生物能源技术领域,具体涉及一种喜温嗜酸硫杆菌去除沼气中硫化氢的方法。The invention belongs to the technical field of bioenergy, and in particular relates to a method for removing hydrogen sulfide in biogas by mesophilic acidophilus thiobacterium.
背景技术Background technique
随着经济的高速发展,世界各地能源需求量日益上升。在能源结构中,以石油、煤炭等为主的化石能源依旧占据着主体地位,人类若过分依赖这些传统化石能源,其不可再生性必将引起能源危机。沼气作为一种新兴的绿色能源逐渐引起人们的重视。沼气是一种混合气体,一般含CH4为60%~70%,CO2为30%~40%,少量的H2S、水汽、NH3等。其中硫化氢对人身安全、环境以及设备都有较大的危害。对于人身安全,硫化氢对粘膜有较强的刺激作用,是强烈的神经毒物。对于环境而言,硫化氢对水体和空气都有污染,燃烧产生的二氧化硫导致酸雨的产生。对于设备,在原油开采,储备运输和加工过程中具有腐蚀危害,严重会造成重大安全事故。沼气用途不同,对H2S含量的要求也不同,相应国家及行业标准规定:若利用沼气发电,则H2S的浓度需小于等于200~300mg/m3;若将沼气作为车用燃料或并入燃气管网,则H2S的浓度需小于等于15 mg/m3。沼气中H2S的质量浓度一般为1~12g/m3,远远超过标准中的规定,若不进行预处理,沼气中含有的 H2S会腐蚀金属管道、仪器仪表等。因此,沼气在综合利用前必须进行H2S脱除。With the rapid development of the economy, the demand for energy around the world is increasing day by day. In the energy structure, fossil energy such as oil and coal still occupies a dominant position. If human beings rely too much on these traditional fossil energy, their non-renewability will definitely cause an energy crisis. As a new green energy, biogas has gradually attracted people's attention. Biogas is a mixed gas, which generally contains 60%~70% CH4 , 30%~40 % CO2 , and a small amount of H2S, water vapor, NH3 , etc. Among them, hydrogen sulfide is harmful to personal safety, environment and equipment. For personal safety, hydrogen sulfide has a strong stimulating effect on mucous membranes and is a strong nerve poison. As far as the environment is concerned, hydrogen sulfide pollutes water bodies and air, and sulfur dioxide produced by combustion leads to acid rain. For equipment, there are corrosion hazards in the process of crude oil extraction, storage, transportation and processing, which may cause major safety accidents. Different uses of biogas have different requirements for H 2 S content. The corresponding national and industry standards stipulate that: if biogas is used for power generation, the concentration of H 2 S must be less than or equal to 200~300mg/m 3 ; if biogas is used as vehicle fuel or Incorporated into the gas pipeline network, the concentration of H 2 S must be less than or equal to 15 mg/m 3 . The mass concentration of H 2 S in biogas is generally 1~12g/m 3 , far exceeding the standard. If no pretreatment is carried out, the H 2 S contained in biogas will corrode metal pipes, instruments and meters. Therefore, H 2 S must be removed before comprehensive utilization of biogas.
无论是国内还是国外,硫化氢脱除方法都有不少,简单的可以分为湿法脱硫、干法脱硫和生物脱硫。湿法脱硫是通过氢氧化钠、氨水等特定的溶剂,与硫化氢反应来脱除硫化氢的一种方法,通过氧气对溶剂的作用达到溶剂的循环利用。由于氢氧化钠的流速和流量的影响,硫化氢并不能完全溶解在起其中,并在溶解过程中会产生硫代硫酸盐,这些都将影响脱硫效果,而且还有投资多、运行管理复杂、脱硫成本高和吸收液需更换等问题。干法脱硫是一种利用氧气,以氧化铁作为氧化剂将硫化氢氧化为单质硫或者硫化物的一种脱硫方式。单质硫在吸收过程中起到了一个催化的作用。但干法脱硫技术有装置占地面积大、操作不连续、脱硫剂不易再生、不易更换和脱硫效率低等问题。生物脱硫技术是通过微生物代谢途径将H2S转化为硫酸盐或者单质硫的一种脱除技术。但其脱硫的稳定性容易受到环境温度的影响。Whether domestic or foreign, there are many methods for hydrogen sulfide removal, which can be simply divided into wet desulfurization, dry desulfurization and biological desulfurization. Wet desulfurization is a method of removing hydrogen sulfide by reacting specific solvents such as sodium hydroxide and ammonia water with hydrogen sulfide. The solvent is recycled through the action of oxygen on the solvent. Due to the influence of the flow rate and flow rate of sodium hydroxide, hydrogen sulfide cannot be completely dissolved in it, and thiosulfate will be produced during the dissolution process, which will affect the desulfurization effect, and there are many investment, complicated operation and management, There are problems such as high desulfurization cost and the need to replace the absorption liquid. Dry desulfurization is a desulfurization method that uses oxygen and iron oxide as an oxidant to oxidize hydrogen sulfide into elemental sulfur or sulfide. Elemental sulfur plays a catalytic role in the absorption process. However, the dry desulfurization technology has problems such as large equipment area, discontinuous operation, difficult regeneration and replacement of desulfurizer, and low desulfurization efficiency. Biological desulfurization technology is a removal technology that converts H 2 S into sulfate or elemental sulfur through microbial metabolic pathways. However, its desulfurization stability is easily affected by the ambient temperature.
硫化物氧化菌主要分为三类:丝状硫细菌、光合硫细菌和无色硫细菌,大部分属于化能自养型。其中硫杆菌属是土壤和自然水体中最常见的一种无色硫细菌,一般为无芽孢的短杆菌,革兰氏阴性,端生鞭毛,能将硫化物氧化成单质硫或硫酸盐,或将硫代硫酸盐氧化为硫酸盐。迄今为止,人们已经证实硫杆菌属有8种:氧化硫硫杆菌,排硫硫杆菌,脱氮硫杆菌,氧化亚铁硫杆菌,那不勒斯硫杆菌,新型硫杆菌,中间硫杆菌和代谢不全硫杆菌。其中前4种在硫酸盐废水处理研究中应用最为广泛。Sulfide-oxidizing bacteria are mainly divided into three categories: filamentous sulfur bacteria, photosynthetic sulfur bacteria and colorless sulfur bacteria, most of which are chemoautotrophic. Among them, Thiobacillus is the most common colorless sulfur bacteria in soil and natural water. It is generally a sporeless brevibacterium, Gram-negative, with terminal flagella, and can oxidize sulfide into elemental sulfur or sulfate, or Oxidizes thiosulfate to sulfate. So far, eight species of Thiobacillus have been identified: Thiobacillus thiooxidans, Thiobacillus thiaulans, Thiobacillus denitrificans, Thiobacillus ferrooxidans, Thiobacillus naples, Thiobacillus neoformans, Thiobacillus intermedius and Thiobacillus incomplete metabolism . Among them, the first four are most widely used in the research of sulfate wastewater treatment.
喜温嗜酸硫杆菌(Acidithiobacillus caldus)是嗜酸硫杆菌属(Acidithiobacillus)中惟一的适度嗜热菌,嗜酸好氧,是一种化能自养的革兰氏阴性菌,以硫或还原性的硫化物为能量来源,以空气中的 CO2为碳源,并吸收氮、磷等无机营养物质合成菌体细胞,一般会将硫粉、HS-和 H2S氧化H2SO4。 Acidithiobacillus caldus is the only moderately thermophilic bacterium in the genus Acidithiobacillus . It is acidophilic and aerobic. The active sulfide is used as the energy source, CO 2 in the air is used as the carbon source, and inorganic nutrients such as nitrogen and phosphorus are absorbed to synthesize bacterial cells. Generally, sulfur powder, HS - and H 2 S are oxidized to H 2 SO 4 .
发明内容Contents of the invention
本发明的目的是提供一种喜温嗜酸硫杆菌去除沼气中硫化氢的方法,具有操作方便,工艺流程简单,提高资源利用价值,节省费用、提高脱硫效率等优点,可以稳定高效地脱除沼气中的硫化氢,将有助于提高沼气利用水平,突破沼气脱硫难题。The purpose of the present invention is to provide a method for removing hydrogen sulfide in biogas by mesophilic acidophilic thiobacillus, which has the advantages of convenient operation, simple process flow, improved resource utilization value, cost saving, and improved desulfurization efficiency, etc., and can remove hydrogen sulfide stably and efficiently The hydrogen sulfide in biogas will help to improve the utilization level of biogas and break through the problem of biogas desulfurization.
本发明所采用的技术方案是:The technical scheme adopted in the present invention is:
喜温嗜酸硫杆菌去除沼气中硫化氢的方法的具体操作步骤如下:The specific operation steps of the method for removing hydrogen sulfide in biogas by mesophilic acidophilus thiobacillus are as follows:
1)反应器A为产沼气装置;1) Reactor A is a biogas generating device;
2)喜温嗜酸硫杆菌生物脱硫装置B中装有9K培养基和3%~5%接种量的喜温嗜酸硫杆菌,进行喜温嗜酸硫杆菌去除沼气中硫化氢;2) Thermophilic Thiobacillus biological desulfurization device B is equipped with 9K medium and 3%~5% inoculum of Thermophilic Thiobacillus, to remove hydrogen sulfide from biogas by Thermophilic Thiobacillus;
3)每天检测一次喜温嗜酸硫杆菌去除沼气中的硫化氢装置中硫化氢浓度的变化;3) Detect once a day the change of the concentration of hydrogen sulfide in the device for removing hydrogen sulfide from biogas by mesophilic acidophilus thiobacillus;
步骤1)产沼气的反应器A中沼气发酵原料包括有机废水、畜禽粪便、生活垃圾和秸秆等。Step 1) Biogas fermentation raw materials in biogas-producing reactor A include organic waste water, livestock and poultry manure, domestic garbage and straw, etc.
步骤1)所述产沼气的反应器A中沼气发酵液产沼气的硫化氢浓度为1000ppm~2000ppm。Step 1) The hydrogen sulfide concentration of the biogas fermentation liquid in the biogas-producing reactor A is 1000ppm-2000ppm.
步骤2)所述喜温嗜酸硫杆菌的培养基配方为:A:硫酸铵3.0 g,氯化钾0.1 g,磷酸氢二钾0.5 g,七水硫酸镁0.5 g,硝酸钙0.01 g,蒸馏水1L,用稀硫酸将pH调至2.5,高压灭菌20min。B:硫酸亚铁3~4%,蒸馏水10mL,过膜除菌。接种前将B加入到A培养基中。Step 2) The medium formula of the mesophilic acidophilus thiobacterium is: A: 3.0 g ammonium sulfate, 0.1 g potassium chloride, 0.5 g dipotassium hydrogen phosphate, 0.5 g magnesium sulfate heptahydrate, 0.01 g calcium nitrate, distilled water 1L, adjust the pH to 2.5 with dilute sulfuric acid, and autoclave for 20 minutes. B: Ferrous sulfate 3~4%, distilled water 10mL, pass membrane to sterilize. Add B to A medium before inoculation.
步骤2)所述采用9K培养基将喜温嗜酸硫杆菌培养至对数期,取少量菌液做活细胞计数,测得菌种活细胞数为2.0×106个/mL~10.0×106个/mL。Step 2 ) The 9K culture medium was used to cultivate the mesophilic acidophilic thiobacterium to the logarithmic phase, and a small amount of bacterial liquid was taken to count the viable cells. individual/mL.
步骤2)所述沼气经过装有喜温嗜酸硫杆菌菌液的反应器B进行生物脱硫后硫化氢浓度不超过30ppm,优选的低于10ppm。Step 2) The hydrogen sulfide concentration after the biogas passes through the reactor B equipped with the mesophilic acidophilus thiobacillus liquid for biological desulfurization is not more than 30ppm, preferably lower than 10ppm.
所述喜温嗜酸硫杆菌为中国微生物菌种保藏中心保藏的菌种编号为1.7296的菌株,喜温嗜酸硫杆菌(Acidithiobacillus caldus)是一类专性自养极端嗜酸性硫杆菌,广泛分布于硫化矿床、酸性矿水及土壤中,在细菌冶金、煤的脱硫和含硫废水的处理等方面发挥重要作用,同时在自然界的硫循环中也占有重要地位。Dopson和Lindtrom研究分析了喜温嗜酸硫杆菌的代谢物具有表面活性剂的作用,使硫元素能充分得到溶解。喜温嗜酸硫杆菌氧化能力很强,细胞增长1g便可生成20g以上的单质硫,将待处理的沼气连续的通入到喜温嗜酸硫杆菌的发酵液中,根据沼气的通入速率调节发酵液的用量,以收集的沼气中硫化氢含量符合所需目标为基准,根据处理量目标调节。The mesophilic acidophilic thiobacillus is a bacterial strain with a strain number of 1.7296 preserved by the China Microorganism Culture Collection Center. In sulfide deposits, acid mineral water and soil, it plays an important role in bacterial metallurgy, coal desulfurization and treatment of sulfur-containing wastewater, and also plays an important role in the natural sulfur cycle. Dopson and Lindtrom studied and analyzed that the metabolites of mesophilic acidophilus Thiobacillus have the effect of surfactant, so that sulfur can be fully dissolved. The mesophilic acidophilic thiobacterium has a strong oxidation ability, and the cell growth of 1g can generate more than 20g of elemental sulfur. Adjust the amount of fermentation broth, based on the hydrogen sulfide content in the collected biogas meeting the required target, and adjust according to the treatment capacity target.
所述菌株的培养方法为:将喜温嗜酸硫杆菌菌株进行恢复培养,用无菌吸管吸取0.3~0.5mL的9K培养基,滴入安瓿内,轻轻震荡,使冻干菌体溶解呈悬浮状,吸取全部菌悬液,移至5mL的9K培养基中,置搅拌速度170 r/min,温度40~45℃培养48~72h,由于菌种经过冷冻干燥保存后,延迟期较长,将一代恢复培养的喜温嗜酸硫杆菌培养液按3%~5%的接种量接种到5mL液体培养基中,同样的培养条件进行连续两次的继代培养,将恢复培养的喜温嗜酸硫杆菌培养液按3%~5%的接种量接种到80mL液体培养基中,同样的培养条件将喜温嗜酸硫杆菌培养至对数期中期(4~5d)。将沼气通入到喜温嗜酸硫杆菌的发酵液中进行脱硫,脱硫过程控制搅拌速度为170 r/min,温度40~45℃。The cultivation method of the strain is as follows: carry out recovery culture of the mesophilic acidophilus Thiobacillus strain, absorb 0.3-0.5mL of 9K medium with a sterile pipette, drop it into the ampoule, shake gently, and dissolve the freeze-dried bacteria into a Suspended, absorb all the bacterial suspension, transfer it to 5mL of 9K medium, set the stirring speed at 170 r/min, and incubate at 40-45°C for 48-72h. Since the bacteria are stored in a freeze-dried manner, the delay period is relatively long. Inoculate the first-generation mesophilic acidophilic thiobacillus culture solution into 5mL liquid medium at an inoculum volume of 3% to 5%, and carry out two consecutive subcultures under the same culture conditions. Acidthiobacillus culture solution was inoculated into 80mL liquid medium at an inoculum volume of 3%~5%, and the mesophilic acidthiobacillus was cultured to the mid-logarithmic phase (4~5d) under the same culture conditions. The biogas was passed into the fermentation broth of mesophilic acidophilus thiobacterium for desulfurization. During the desulfurization process, the stirring speed was controlled at 170 r/min and the temperature was 40-45°C.
本发明具有的积极效果是:由于本发明是采用喜温嗜酸硫杆菌去除沼气中的硫化氢,从而显著减少了原位沼气中硫化氢的量,脱除对环境以及设备有危害的硫化氢,脱除效率高,减少了后续脱硫的费用和工作量。喜温嗜酸硫杆菌氧化能力很强,细胞增长1g便可生成20g以上的单质硫,李亚新等通过好氧无色硫细菌生物膜反应器,开展了硫化物转化成单质硫的实验,硫化氢的去除率达87%,本发明脱硫效率达98.24%,远远超过现有技术的脱硫效率。The positive effects of the present invention are: because the present invention uses mesophilic acidophilic thiobacterium to remove hydrogen sulfide in biogas, thereby significantly reducing the amount of hydrogen sulfide in in-situ biogas, and removing hydrogen sulfide that is harmful to the environment and equipment , high removal efficiency, reducing the cost and workload of subsequent desulfurization. Thermophilic Acidophilus Thiobacillus has a strong oxidizing ability, and more than 20 g of elemental sulfur can be produced by 1 g of cell growth. Li Yaxin et al. carried out experiments on the conversion of sulfide into elemental sulfur through an aerobic colorless sulfur bacteria biofilm reactor. Hydrogen sulfide The removal rate reaches 87%, and the desulfurization efficiency of the present invention reaches 98.24%, far exceeding the desulfurization efficiency of the prior art.
附图说明Description of drawings
图1为反应装置示意图;Fig. 1 is the schematic diagram of reaction device;
图2为喜温嗜酸硫杆菌脱硫的硫化氢浓度变化曲线。Figure 2 is the hydrogen sulfide concentration change curve for desulfurization by mesophilic acidophilus Thiobacillus.
具体实施方式detailed description
下面结合附图,对本发明具体实施方式进行详细说明。The specific embodiments of the present invention will be described in detail below in conjunction with the accompanying drawings.
所述喜温嗜酸硫杆菌为中国微生物菌种保藏中心保藏的菌种编号为1.7296的菌株。The mesophilic acidophilic Thiobacillus is a strain with a strain number of 1.7296 preserved in the China Microorganism Culture Collection Center.
实施例1Example 1
本实施例提供一种加入喜温嗜酸硫杆菌菌株进行去除沼气中硫化氢的实验。This example provides an experiment for removing hydrogen sulfide in biogas by adding a strain of mesophilic acidophilus Thiobacillus.
步骤一,将喜温嗜酸硫杆菌菌株进行恢复培养,用无菌吸管吸取0.3~0.5mL的9K培养基,滴入安瓿内,轻轻震荡,使冻干菌体溶解呈悬浮状,吸取全部菌悬液,移至5mL的9K培养基中,置搅拌速度170 r/min,温度40~45℃培养48~72h,由于菌种经过冷冻干燥保存后,延迟期较长,将一代恢复培养的喜温嗜酸硫杆菌培养液按3%~5%的接种量接种到5mL液体培养基中,同样的培养条件进行连续两次的继代培养,将恢复培养的喜温嗜酸硫杆菌培养液按3%~5%的接种量接种到80mL液体培养基中,同样的培养条件将喜温嗜酸硫杆菌培养至对数期中期(4~5d)。喜温嗜酸硫杆菌的培养基配方为:A:硫酸铵3.0 g,氯化钾0.1 g,磷酸氢二钾0.5 g,七水硫酸镁0.5 g,硝酸钙0.01 g,蒸馏水1L,用稀硫酸将pH调至2.5,高压灭菌20min。B:硫酸亚铁3~4%,蒸馏水10mL,过膜除菌。接种前将B加入到A培养基中。Step 1: Carry out recovery culture of mesophilic acidophilus Thiobacillus strain, draw 0.3~0.5mL of 9K medium with a sterile pipette, drop it into the ampoule, shake gently, so that the freeze-dried bacteria dissolve and form a suspension, absorb all The bacterial suspension was transferred to 5 mL of 9K medium, and the stirring speed was 170 r/min, and the temperature was 40-45 ° C for 48-72 hours. Since the strains were stored in freeze-drying, the lag period was long, so the cultured one generation The mesophilic acidophilus thiobacillus culture solution was inoculated into 5mL liquid medium at an inoculum volume of 3%~5%, and the same culture conditions were carried out for two consecutive subcultures, and the recovered mesophilic acidophilus thiobacillus culture solution Inoculate 3%~5% of the inoculum into 80mL liquid medium, and culture the mesophilic acidophilus Thiobacillus to the mid-logarithmic phase (4~5d) under the same culture conditions. The medium formula of thermophilic acidophilus thiobacterium is: A: 3.0 g ammonium sulfate, 0.1 g potassium chloride, 0.5 g dipotassium hydrogen phosphate, 0.5 g magnesium sulfate heptahydrate, 0.01 g calcium nitrate, 1 L distilled water, dilute sulfuric acid Adjust the pH to 2.5 and autoclave for 20 minutes. B: Ferrous sulfate 3~4%, distilled water 10mL, pass membrane to sterilize. Add B to A medium before inoculation.
步骤二,沼气生产:使用酒精废水化学需氧量(COD)是29,000 mg/L,pH 是3.78,总氮是74.84 mg/L,总挥发性脂肪酸(VFAs)是21.45 mM,活性污泥可挥发性悬浮固体VSS(36.49 g /L)的发酵液作为沼气生产的原料;Step 2, biogas production: the chemical oxygen demand (COD) of alcohol wastewater is 29,000 mg/L, the pH is 3.78, the total nitrogen is 74.84 mg/L, the total volatile fatty acids (VFAs) are 21.45 mM, and the activated sludge can be volatilized The fermentation broth of VSS (36.49 g/L) was used as raw material for biogas production;
步骤三,取2组装置,编号A0和A1,两个装置A装置加入80mL步骤二所得的发酵液,编号A1的脱硫装置的反应器B中加入80mL的9K培养基,接种3%~5%步骤一所得的喜温嗜酸硫杆菌菌液;Step 3, take 2 sets of devices, numbered A0 and A1, add 80mL of the fermentation broth obtained in step 2 to the two devices A, add 80mL of 9K medium to the reactor B of the desulfurization device numbered A1, and inoculate 3%~5% The mesophilic acidophilus bacterium liquid obtained in step one;
步骤四,将A0和A1号装置放入转速为170 r/min摇床中,温度40 ℃,进行反应,反应6天,并记录硫化氢浓度的变化。Step 4: Put devices A0 and A1 into a shaker with a rotation speed of 170 r/min and a temperature of 40 °C to react for 6 days, and record the change of hydrogen sulfide concentration.
从图2可以得出对照样不加入喜温嗜酸硫杆菌硫化氢浓度为1423.05 ppm,添加喜温嗜酸硫杆菌的脱硫装置第一天产生的沼气中硫化氢的浓度为22.41 ppm,第六天产生的沼气中硫化氢的浓度为5.93 ppm,脱硫效果明显。可见,喜温嗜酸硫杆菌使硫化氢的含量有明显下降,硫化氢的脱除效果比较好。From Figure 2, it can be concluded that the concentration of hydrogen sulfide in the control sample without adding mesophilic thiobacterium was 1423.05 ppm, and the concentration of hydrogen sulfide in the biogas produced by the desulfurization device added with mesophilic thiobacterium was 22.41 ppm on the first day, and the concentration of hydrogen sulfide in the sixth day was 22.41 ppm. The concentration of hydrogen sulfide in the biogas produced every day is 5.93 ppm, and the desulfurization effect is obvious. It can be seen that the mesophilic acidophilus Thiobacillus can significantly reduce the content of hydrogen sulfide, and the removal effect of hydrogen sulfide is better.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611010804.5A CN106635210B (en) | 2016-11-17 | 2016-11-17 | A method for removing hydrogen sulfide in biogas by mesophilic acidophilic thiobacillus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611010804.5A CN106635210B (en) | 2016-11-17 | 2016-11-17 | A method for removing hydrogen sulfide in biogas by mesophilic acidophilic thiobacillus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106635210A true CN106635210A (en) | 2017-05-10 |
| CN106635210B CN106635210B (en) | 2019-08-16 |
Family
ID=58807280
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611010804.5A Active CN106635210B (en) | 2016-11-17 | 2016-11-17 | A method for removing hydrogen sulfide in biogas by mesophilic acidophilic thiobacillus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106635210B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108159871A (en) * | 2017-12-30 | 2018-06-15 | 常州水精灵环保设备有限公司 | A kind of preparation method of composite desulfurizing agent |
| CN109939558A (en) * | 2017-12-21 | 2019-06-28 | 南京蓝色气候能源技术有限公司 | A kind of method of biogas desulfurization |
| CN114618279A (en) * | 2022-04-12 | 2022-06-14 | 同济大学 | Emission reduction system and construction method for removing odor and greenhouse gas using sulfur autotrophs |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101200698A (en) * | 2007-11-26 | 2008-06-18 | 宁波工程学院 | A kind of microorganism that simultaneously removes ammonia and hydrogen sulfide malodorous gas and its preparation method |
| CN103937576A (en) * | 2014-05-02 | 2014-07-23 | 中南大学 | Efficient biological desulfurization method for coal |
-
2016
- 2016-11-17 CN CN201611010804.5A patent/CN106635210B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101200698A (en) * | 2007-11-26 | 2008-06-18 | 宁波工程学院 | A kind of microorganism that simultaneously removes ammonia and hydrogen sulfide malodorous gas and its preparation method |
| CN103937576A (en) * | 2014-05-02 | 2014-07-23 | 中南大学 | Efficient biological desulfurization method for coal |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109939558A (en) * | 2017-12-21 | 2019-06-28 | 南京蓝色气候能源技术有限公司 | A kind of method of biogas desulfurization |
| CN108159871A (en) * | 2017-12-30 | 2018-06-15 | 常州水精灵环保设备有限公司 | A kind of preparation method of composite desulfurizing agent |
| CN114618279A (en) * | 2022-04-12 | 2022-06-14 | 同济大学 | Emission reduction system and construction method for removing odor and greenhouse gas using sulfur autotrophs |
| CN114618279B (en) * | 2022-04-12 | 2023-02-21 | 同济大学 | Emission reduction system for removing stink and greenhouse gas by using sulfur autotrophic bacteria and building method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106635210B (en) | 2019-08-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Haosagul et al. | Sulfide-oxidizing bacteria community in full-scale bioscrubber treating H2S in biogas from swine anaerobic digester | |
| CN1155696C (en) | Ferrous oxide theobacillus and sludge heavy-metal eliminating method therewith | |
| CN102583930A (en) | Livestock excrement biogas generation method and livestock excrement biogas generation system | |
| CN106268259B (en) | SO in a kind of flue gas2With the method for Hg biochemical synchronizations removing | |
| CN111760443B (en) | Biological desulfurization active particles capable of realizing flora partition, and preparation method and application thereof | |
| Angenent et al. | Upgrading anaerobic digestion within the energy economy–the methane platform | |
| CN102276118A (en) | Method for simultaneously removing nitrogen in waste water and sulfur in sewage gas | |
| CN101386823B (en) | Special effect anaerobic denitrifying bacterium and waste water processing method using thereof | |
| CN106635210B (en) | A method for removing hydrogen sulfide in biogas by mesophilic acidophilic thiobacillus | |
| CN104911133B (en) | A kind of pseudomonas aeruginosa and application | |
| Song et al. | Air supplement as a stimulation approach for the in situ desulfurization and methanization enhancement of anaerobic digestion of chicken manure | |
| CN104857842B (en) | One plant of thermophilic salt basophilla sulfur oxidizing bacterium and its application in gaseous bio desulfurization-sulfur recovery | |
| CN109593663B (en) | Efficient biological desulfurization microbial inoculum and application method thereof | |
| CN111793573A (en) | A seaweed Shewanella strain with both heterotrophic and autotrophic nitrate dissimilatory reduction functions to ammonium, cultivation method and application thereof | |
| CN116004431B (en) | A strain of Brucella intermedia LW2 and its application | |
| CN106554837B (en) | A method for combined removal of hydrogen sulfide from biogas with iron-containing compound and mesophilic acidophilus thiobacterium | |
| CN111996134A (en) | Halophilic and basophilic sulfur oxidation complex microbial inoculant, preparation method thereof and application thereof in biological desulfurization | |
| CN103966128A (en) | Thiobacillus neapolitanus and application of thiobacillus neapolitanus in biological desulfurization | |
| CN103406007A (en) | Recovery process for sulphur in gold concentrate roasting smoke | |
| Chen et al. | Sulfate removal by Desulfovibrio sp. CMX in chelate scrubbing solutions for NO removal | |
| Li et al. | Synergistic nitrogen removal through sulfate reduction and sulfur autotrophic denitrification driven by sustained-release carbon source in sulfate-rich wastewater | |
| CN118703589A (en) | A method for screening methanol-producing methane-oxidizing bacteria | |
| CN117701444A (en) | Preparation method of magnetic biochar immobilized with ammonia nitrogen-resistant anaerobic microorganisms and method for relieving ammonia nitrogen inhibition | |
| CN104805038A (en) | Acrylic resin degrading bacteria and screening enrichment method thereof | |
| CN111690575B (en) | High-tolerance organic sulfur thermoalcalophilus halophilus, culture method thereof and application thereof in biological desulfurization |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |