DE3912418C1 - Degradation of hydrogen sulphide and fatty acids in bio-gas - by using chromatium species DSM 5080 together with rhodopseudomonas species FDSM 5020 in alkaline culture - Google Patents
Degradation of hydrogen sulphide and fatty acids in bio-gas - by using chromatium species DSM 5080 together with rhodopseudomonas species FDSM 5020 in alkaline cultureInfo
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- DE3912418C1 DE3912418C1 DE3912418A DE3912418A DE3912418C1 DE 3912418 C1 DE3912418 C1 DE 3912418C1 DE 3912418 A DE3912418 A DE 3912418A DE 3912418 A DE3912418 A DE 3912418A DE 3912418 C1 DE3912418 C1 DE 3912418C1
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- 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
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/02—Photobioreactors
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
- C12M23/06—Tubular
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M47/00—Means for after-treatment of the produced biomass or of the fermentation or metabolic products, e.g. storage of biomass
- C12M47/18—Gas cleaning, e.g. scrubbers; Separation of different gases
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- 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
- C12N1/205—Bacterial isolates
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
- C12R2001/00—Microorganisms ; Processes using microorganisms
- C12R2001/01—Bacteria or Actinomycetales ; using bacteria or Actinomycetales
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- 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
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- 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
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- General Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
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- Tropical Medicine & Parasitology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Clinical Laboratory Science (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
Description
Die Erfindung betrifft die Elimination von Schwefelwas serstoff und Gärungsstoffwechselprodukten mittels einer Mischkultur phototropher Bakterien unter anaeroben Be dingungen im Licht und einen bestimmten Mikroorganismus (vgl. die Patentansprüche).The invention relates to the elimination of sulfur Hydrogen and fermentation metabolites by means of a Mixed culture of phototrophic bacteria under anaerobic conditions conditions in light and a specific microorganism (see the claims).
Die bakterielle Mischkultur phototropher Bakterien soll zum einen übelriechende kurzkettige flüchtige Fettsäu ren und zum anderen den Anteil an giftigem korrosivem Schwefelwasserstoff aus dem Biogas anaerob betriebener Bioreaktoren entfernen, um das Gas mit einem Anteil von 75% Methan für eine Verbrennung als auch zur Stromer zeugung mittels Gasmotoren nutzen zu können.The mixed bacterial culture of phototrophic bacteria is said to on the one hand malodorous short-chain volatile fatty acid and the proportion of toxic corrosive Hydrogen sulfide from the biogas operated anaerobically Remove bioreactors to remove the gas with a share of 75% methane for both combustion and electricity generation using gas engines.
Es ist bekannt, den Schwefelwasserstoffanteil im Biogas zu senken, indem entweder durch Zusätze von Schwerme tallen (z. B. Eisen) im Reaktorzulauf eine Sulfidbil dung eingeleitet wird oder über die Zugabe von Luftsau erstoff eine Hemmung des Wachstums desulfurisierender Bakterien herbeigeführt wird oder indem das schwefel wasserstoffhaltige Biogas über eisenhydroxidhaltige Reinigungsmassen geleitet wird oder indem in einem mik robiellen Oxydationsprozeß eine Sulfidoxydation durch geführt wird.It is known the proportion of hydrogen sulfide in biogas to decrease by either adding heavy ingredients a sulfide bilge (e.g. iron) in the reactor feed is initiated or via the addition of air sau inhibiting growth of desulfurizing Bacteria is brought about or by the sulfur biogas containing hydrogen over iron hydroxide Cleaning compounds is passed or by in a mic robust oxidation process through a sulfide oxidation to be led.
Das Verfahren zur Senkung von Schwefelwasserstoff im Biogas durch Zusatz von Schwermetallen im Biogasreaktor hat den Nachteil, daß der Schadstoff im System ver bleibt. Eine Zudosierung von Luftsauerstoff kann in Gegenwart von Methan zu einem explosiven Gemisch führen. Die Prozesse zur Elimination an Raseneisenerz erzeugen Eisensulfid als Abfallstoff. The process for lowering hydrogen sulfide in the Biogas by adding heavy metals in the biogas reactor has the disadvantage that the pollutant ver in the system remains. Air oxygen can be added in the presence of methane to an explosive mixture. Generate the processes for eliminating turf iron ore Iron sulfide as a waste.
Bei der mikrobiellen Sulfidoxydation wird ein sulfathaltiges Abwasser in den Abwasser reinigungsprozeß der Kläranlage zurückgeführt, so daß eine erneute Desulfurikation unter aneroben Bedingungen einsetzen kann.In microbial sulfide oxidation is a sulfate-containing waste water in the waste water cleaning process of the sewage plant returned so that renewed desulfurization under anerobic conditions can use.
Der Erfindung liegt die Aufgabe zugrunde, das entstan dene Biogas einer Anaerob-Anlage mikrobiell mittels einer phototrophen Mischkultur unter aneroben Bedin gungen im Licht von Schwefelwasserstoff und flüchtigen Gärungsstoffwechselprodukten zu reinigen und hierfür geeignete Mikroorganismen zur Verfügung zu stellen. Die Aufgabe wird erfindungsgemäß dadurch gelöst, daß Biogas durch eine alkalische Mischkultur der phototro phen Bakterien geleitet wird (vgl. Patentanspruch 2). Hierbei lösen sich Schwe felwasserstoff, Kohlendioxid und flüchtige organische Fettsäuren in der mineralischen Nährsalzlösung.The invention has for its object that the biogas of an anaerobic plant using microbial agents a phototrophic mixed culture under anerobic conditions in the light of hydrogen sulfide and volatile To clean fermentation metabolism products and to provide suitable microorganisms. The object is achieved in that Biogas through an alkaline mixed culture from phototro phen bacteria is directed (see claim 2). This will loosen sweat hydrogen sulfide, carbon dioxide and volatile organic Fatty acids in the mineral nutrient salt solution.
Der Stamm Chromatium spez. DSM 5083 oxidiert Schwefelwasserstoff anaerob im Licht zu elementarem Schwefel und speichert ihn in dieser Form in der Zelle. Bei Mangel von Schwe felwasserstoff tritt eine weitere Oxidation bei der As similation von Kohlendioxid bis zum Sulfat ein.The strain Chromatium spec. DSM 5083 oxidizes hydrogen sulfide anaerobic in the light to elemental sulfur and stores him in this form in the cell. In the absence of sweat hydrogen sulfide occurs a further oxidation at the As simulation of carbon dioxide to sulfate.
Schwefelwasserstoff kann bis zu einem Konzentrationsbe reich in der Kultur von 7,1 mg/l-14 mg/l verwertet werden. Der Bakterienstamm nutzt vorwiegend Strahlungen im nahen Infrarotbereich zwischen 700-800 nm.Hydrogen sulfide can reach a concentration level richly utilized in the culture of 7.1 mg / l-14 mg / l will. The bacterial strain mainly uses radiation in the near infrared range between 700-800 nm.
Der Stamm Rhodospeudomonas spez. DSM 5020 baut sowohl anaerob im Licht als auch mikroaerob im Dunkeln niedermolekulare organische Abbauprodukte des Gärungsstoffwechsels ab. Ferner ist er in der Lage, Schwefelwasserstoff geringer Konzentration im Bereich von 1,4 mg/l-2,8 mg/l im Licht zu oxidieren. Der dabei entstehende Schwefel wird in die Kultur ausgeschieden und nicht in der Zelle ge speichert. Der Stamm produziert während des Wachstums Biotin, das dem Stamm Chromatium spez. DSM 5083 als Wuchsstoff dient. Rhodopseudomonas spez. DSM 5020 nutzt ebenfalls vorwiegend Strahlungen im nahen Infrarotbereich zwischen 700-900 nm. The strain Rhodospeudomonas spec. DSM 5020 builds both anaerobically in Light as well as microaerobic in the dark low molecular weight organic decomposition products of the fermentation metabolism. He is also able to lower hydrogen sulfide Concentration in the range of 1.4 mg / l-2.8 mg / l im Oxidize light. The resulting sulfur becomes excreted in the culture and not in the cell saves. The strain produces during growth Biotin, the Chromatium spec. DSM 5083 as a growth substance serves. Rhodopseudomonas spec. DSM 5020 also predominantly uses Radiations in the near infrared range between 700-900 nm.
Der mikrobielle Abbau der o. g. Schadstoffe des Biogases in der Kulturlösung erfolgt in einem lichtdurchströmten Röhrenreaktor.The microbial degradation of the above Biogas pollutants in the culture solution takes place in a light-flooded Tube reactor.
Die anschließend schadstofffreie Kulturlösung wird er neut zur Biogaswäsche eingesetzt.It will become the subsequently pollutant-free culture solution now used for biogas washing.
Der Anteil an Schwefelsäure als Endprodukt des mikrobi ellen Abbauprozesses wird dem System durch Bildung von Calciumsulfat entzogen.The proportion of sulfuric acid as the end product of the microbi The degradation process is brought to the system by forming Calcium sulfate withdrawn.
Die mit der Erfindung erzielten Vorteile bestehen ins besondere darin, daß der Prozeß zur Biogasreinigung ge trennt zu dem der Biogaserzeugung abläuft. Auf diese Weise kann der mikrobielle Abbau unter optimierten Bedingungen in einem regel- und steuerbaren Anlagenteil erfolgen.The advantages achieved by the invention are special in that the process for biogas purification ge separates from that of the biogas production. To this Way, the microbial degradation can be optimized under Conditions in an adjustable and controllable part of the system respectively.
Ferner wird der Schwefel dem System durch Erzeugung ei nes wiederverwertbaren Stoffes (als Gips = Calcium sulfat) entzogen.Furthermore, the sulfur is egg to the system by generation recyclable material (as gypsum = calcium sulfate) withdrawn.
Die Anzucht der Bakterien erfolgt in einem Nährmedium:
(mg/l): NaHCO3: 0,8; NH4CL: 0,1; MgSO4 × 7 H2O: 0,08;
CaCl2 × 2 H2O: 0,01; K2HPO4: 0,2; Citronensäure: 0,05;
FeCl3 × 6 H2O: 0,0005; Vitamin B12: 0,0002; Hefeex
trakt: 0,05; Na2S × 9 H2O: 0,25; Na-Acetat: 0,2; Lei
tungswasser.The bacteria are grown in a nutrient medium:
(mg / l): NaHCO 3 : 0.8; NH 4 CL: 0.1; MgSO 4 x 7 H 2 O: 0.08; CaCl 2 × 2 H 2 O: 0.01; K 2 HPO 4 : 0.2; Citric acid: 0.05; FeCl 3 x 6 H 2 O: 0.0005; Vitamin B 12 : 0.0002; Hefeex trakt: 0.05; Na 2 S x 9 H 2 O: 0.25; Na acetate: 0.2; Tap water.
Die statische Kultivierung wird in hoher Schicht bei einer Temperatur von 22-28°C, einem pH-Wert von 7- 7,5 und einer Beleuchtungsstärke von 500-1000 Lux im Lichtspektrum einer Wolframglühlampe durchgeführt.The static cultivation is applied in a high layer a temperature of 22-28 ° C, a pH of 7- 7.5 and an illuminance of 500-1000 lux in Light spectrum of a tungsten incandescent lamp carried out.
Die Anzuchtdauer beträgt 72 Stunden.The cultivation period is 72 hours.
Methangas aus einem anaeroben Prozeßreaktor wird durch die bakterielle Mischkultur mit einem pH-Wert von 7,5-9 geführt. Hierbei werden die Schwefelwasser stoffanteile (H2S) des Biogases, das Kohlendioxid (CO2) und die kurzkettigen organischen Fettsäuren in der mineralischen Nährlösung gelöst.Methane gas from an anaerobic process reactor is passed through the mixed bacterial culture with a pH of 7.5-9. The hydrogen sulfide (H 2 S) components of the biogas, the carbon dioxide (CO 2 ) and the short-chain organic fatty acids are dissolved in the mineral nutrient solution.
Zur Erzeugung von Wachstum und Elimination der Schad stoffe fließt die beladene Mischkultur im Kreis über einen Bypass durch einen lichtbestrahlten Röhrenreak tor (500-1000 Lux, Wolframlampenlicht) in einem temperierten Teilbereich der Anlage.To generate growth and elimination of harm the mixed culture loaded overflows in a circle a bypass through a light-irradiated tube craze tor (500-1000 lux, tungsten lamp light) in one tempered section of the system.
Nach Durchlauf des Röhrenreaktors sind die o. g. Schad stoffe mikrobiell abgebaut, so daß die Nährlösung er neut im Gaswaschanlagenteil beladen werden kann. Der pH- Wert, Temperatur, Nährsalzgehalt oder Mischkultur in der Anlage werden überwacht und geregelt.After passing through the tube reactor, the above-mentioned. Harmful substances degraded microbially so that the nutrient solution can be reloaded in the gas scrubber section. The pH Value, temperature, nutrient salt content or mixed culture in of the plant are monitored and regulated.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3912418A DE3912418C1 (en) | 1989-04-12 | 1989-04-12 | Degradation of hydrogen sulphide and fatty acids in bio-gas - by using chromatium species DSM 5080 together with rhodopseudomonas species FDSM 5020 in alkaline culture |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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DE3912418A DE3912418C1 (en) | 1989-04-12 | 1989-04-12 | Degradation of hydrogen sulphide and fatty acids in bio-gas - by using chromatium species DSM 5080 together with rhodopseudomonas species FDSM 5020 in alkaline culture |
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DE3912418C1 true DE3912418C1 (en) | 1990-07-12 |
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DE3912418A Expired - Fee Related DE3912418C1 (en) | 1989-04-12 | 1989-04-12 | Degradation of hydrogen sulphide and fatty acids in bio-gas - by using chromatium species DSM 5080 together with rhodopseudomonas species FDSM 5020 in alkaline culture |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0498519A2 (en) * | 1991-02-08 | 1992-08-12 | HERBST UMWELTTECHNIK GmbH | Process for the purification of gases |
EP1970434A1 (en) * | 2007-03-15 | 2008-09-17 | MT-Energie GmbH & Co. KG | Method for reducing hydrogen sulphide by introducing oxygen |
EP3000872A1 (en) | 2014-09-26 | 2016-03-30 | Politechnika Lódzka | Microbiological medium for a microbiological consortium applied in the technology of biological purification of biogas |
-
1989
- 1989-04-12 DE DE3912418A patent/DE3912418C1/en not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
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NICHTS ERMITTELT * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0498519A2 (en) * | 1991-02-08 | 1992-08-12 | HERBST UMWELTTECHNIK GmbH | Process for the purification of gases |
EP0498519A3 (en) * | 1991-02-08 | 1992-09-16 | Herbst Umwelttechnik Gmbh | Process and apparatus for the purification of gases |
EP1970434A1 (en) * | 2007-03-15 | 2008-09-17 | MT-Energie GmbH & Co. KG | Method for reducing hydrogen sulphide by introducing oxygen |
EP3000872A1 (en) | 2014-09-26 | 2016-03-30 | Politechnika Lódzka | Microbiological medium for a microbiological consortium applied in the technology of biological purification of biogas |
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