[go: up one dir, main page]

DE2931380A1 - Farmyard manure gas generator - combining antechamber, fermentation and sealing tank in one compact unit - Google Patents

Farmyard manure gas generator - combining antechamber, fermentation and sealing tank in one compact unit

Info

Publication number
DE2931380A1
DE2931380A1 DE19792931380 DE2931380A DE2931380A1 DE 2931380 A1 DE2931380 A1 DE 2931380A1 DE 19792931380 DE19792931380 DE 19792931380 DE 2931380 A DE2931380 A DE 2931380A DE 2931380 A1 DE2931380 A1 DE 2931380A1
Authority
DE
Germany
Prior art keywords
fermentation
antechamber
biomass
tank
combining
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.)
Ceased
Application number
DE19792931380
Other languages
German (de)
Inventor
Heinz Sauff
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SAUFF HEINZ 4000 DUESSELDORF DE
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to DE19792924387 priority Critical patent/DE2924387A1/en
Application filed by Individual filed Critical Individual
Priority to DE19792931380 priority patent/DE2931380A1/en
Publication of DE2931380A1 publication Critical patent/DE2931380A1/en
Ceased legal-status Critical Current

Links

Classifications

    • 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
    • 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
    • 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
    • C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/18—External loop; Means for reintroduction of fermented biomass or liquid percolate
    • 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
    • C12M45/00—Means for pre-treatment of biological substances
    • C12M45/20—Heating; Cooling
    • 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
    • C12N1/12—Unicellular algae; Culture media therefor
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Genetics & Genomics (AREA)
  • Biotechnology (AREA)
  • Microbiology (AREA)
  • General Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Biomedical Technology (AREA)
  • Sustainable Development (AREA)
  • Molecular Biology (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Cell Biology (AREA)
  • Medicinal Chemistry (AREA)
  • Botany (AREA)
  • Virology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The Parent Patent No. 2924387 described a plant for farmyard manure gas to be used in IC engines or gas burners. It is now suggested to combine the antechamber, the fermentation tank and the settling tank into one large tank with horizontal partitions. The biogenic matter, consisting of solid and liq. manure, is homogenised until it can be pumped and is heated by hot water instead of a heat exchanger. This is a more compact system which is easier to transport and to erect. The antechamber is now always preheated.

Description

Anlage mit Vorrichtungen zur Methangaserzeugung aus System with devices for methane gas generation

organischen Reststoffen Em Gegensatz zu Nr. P 29 24 387.6 handelt es sich hierbei im eine Biogasanlage in der Vorbehälter, Gärbehälter und xbsetzbehälter in einem großen Behälter zusammengefaßt sind. organic residues in contrast to No. P 29 24 387.6 There is a biogas plant in the pre-tank, fermentation tank and settling tank are combined in a large container.

Ion unten nach oben gesehen haben wir die Reihenfolge; Absetzbehälter, Vorbehälter und darüber den Gärbehälter.Looking up at the bottom we have the order; Sedimentation tank, Pre-tank and above the fermentation tank.

Die Abläufe sind die gleichen: frischgut in den Vorbeh0lter, mit- der Pumpe auf millimetergröße zerkleinern, auf die gewünschte Temperatur 34°C, 54° C oder 65° C bringen entweder durch entsprechend warmen wasser oder über einen Wärmetauscher. Danach Beförderung Ln den Gärbehälter. Die Verweildauer beträgt bei den oben angegebenen Temperaturen 19, 9, 3 Tage. Nach dem erstmaligen Auffüllen wird dann tjglich kontinuierlich die zugegebene Menge an ausgefaultem Gut in den Absetzbehälter abge-Weben. Dies wird dann in einem festgelegten Rythmus geleert.The processes are the same: fresh food in the reservoir, with the pump to millimeter size, to the desired temperature 34 ° C, 54 ° C or 65 ° C bring either warm water or a heat exchanger. Then conveyance Ln the fermentation tank. The length of stay is for the ones specified above Temperatures 19, 9, 3 days. After filling up for the first time, it will be continuous every day Weave the added amount of decomposed material into the sedimentation tank. this is then emptied in a fixed rhythm.

bei den Temperaturen von 540 C oder 65° C kann im Absetzbehälter über Wärmetauscher die Wärme wieder rückgewonnen ierden und im Haus verbraucht werden.at temperatures of 540 C or 65 ° C can be in the sedimentation tank over Heat exchangers recover the heat and use it in the house.

ie Vorteile gegenüber Nr@ P 29 24 387.6 sind; les kompakte in einem Großbehälter untergebrachte System daher weniger Linzelteile, bessere Transportmöglichkeiten, im Vorbehulter für das Frischgut herrscht immer eine sehr hohe Temperatur, dadurch Vorerwärmung des eingefüllten Frischgutes.The advantages over Nr @ P 29 24 387.6 are; les compact in one Large tank housed system therefore fewer items, better ones There is always a lot of transport options in the Vorbehulter for the fresh goods high temperature, thereby preheating the fresh food.

Wenn das Frischgut mit warmen Wasser auf Temperatur gebracht wird muß statt der erforderlichen Menge 1/3 oder 1j4 weniger Wasser genommen werden, beim Frischgut einfüllen, das restliche 1/3 oder 1/4 wird bei den erforderlichen Umwälzungen bei Temperaturabfall um 20 C zur Temperaturerhöhung verwand.When the fresh food is brought to temperature with warm water 1/3 or 1j4 less water must be used instead of the required amount, Fill with fresh food, the remaining 1/3 or 1/4 is used for the required Circulations when the temperature dropped by 20 C was used to increase the temperature.

Sie kann als Kleinanlagen ab lo Rinder und zum sofortigen Gasverbrauch über einen Gasbrenner im Haushalt in bestehenden Gas- und Oelkessel verarbeitet werden.It can be used as a small system from lo cattle and for immediate gas consumption processed via a gas burner in the household in existing gas and oil boilers will.

An Hand des gezeichneten Ausführungsbeispieles wird die Erfindung erläutert.The invention is based on the illustrated embodiment explained.

In der Figur l wird die gesamte Biogasanlage als flächiges Gebilde dargestellt.In the figure l, the entire biogas plant is shown as a flat structure shown.

Punkt 1 zeigt die verschließbare Einfüllöffnung für die Biomasse.Point 1 shows the closable filling opening for the biomass.

Punkt 2 zeigt den Vorbehäl-ter, in dem die Biomasse vorbereitet wird.Point 2 shows the container in which the biomass is prepared.

Punkt 3 zeigt das Transportrohr durch daß das auf die gewünschte Temperatur gebrachte Wasser in den Vorbehälter eingebracht wird.Point 3 shows the transport tube through that to the desired temperature brought water is introduced into the holding tank.

Punkt 4 zeigt den Hornogenisator, der die Biomasse auf Millimetergröße homogenisiert und nach der Erwermung durch das Förderrohr Punkt 5, durch das Motorventil Punkt 5, über das Förderrohr Punkt 7 in den Gärbehälter Punkt 8 pumpt.Point 4 shows the hornogenizer, which reduces the biomass to millimeter size homogenized and after heating through the delivery pipe point 5, through the motor valve Point 5, pump point 7 into the fermentation tank point 8 via the delivery pipe.

Sobald die Temperatur im Gärbehälter um 20 C absinkt, öffnet das Motorventil 10, de Ablaufrohre 9 u. 11 und die Biomasse läuft vom Gärbehälter 8 wieder in den Vorhehälter 2 und wird mit dem Warmwasser aus Förderrohr 3 auf die erforderliche Temperatur gebracht und über den omogenisator 4 durch das Förderrohr 5, durch das Motorventil 6, durch das Förderrohr 12 und über die Düsen 13 in den Gdrbehälter 8 gepumpt und zerreißt eine sich eventuell bildende Schwimmdecke.As soon as the temperature in the fermentation tank drops by 20 C, the motor valve opens 10, de drain pipes 9 and 11 and the biomass runs from the fermentation tank 8 again in the Vorhehälters 2 and is with the hot water from the delivery pipe 3 on the brought the required temperature and via the omogenizer 4 through the conveyor pipe 5, through the engine valve 6, through the delivery pipe 12 and through the nozzles 13 into the Gdr container 8 is pumped and tears a floating cover that may be formed.

Ueber das Förderrohr 9, dem Motorventil lo und das Förderrohr 14 wird die täglich anfallende Menge Faulgut in den Behälter 15 abgelassen und über ein Wärmetauschersystem 16 abgekühlt und nach Abkühlung über ein Ventil in den Absetzbehälter 18 abgelassen.About the delivery pipe 9, the engine valve lo and the delivery pipe 14 is drained the daily amount of putrefactive material into the container 15 and over a Heat exchanger system 16 cooled and, after cooling, via a valve into the settling tank 18 drained.

Das ausgefaulte Gut aus Behälter 18 wird über das Transport, rohr 19 nach Füllung abgesaugt.The digested material from container 18 is on the transport, pipe 19 sucked off after filling.

Punkt 20 zeigt die Isolierung, die zur armhaltung des Behälterinhaltes erforderlich ist.Point 20 shows the insulation that is used to hold the contents of the tank by arms is required.

Punkt 21 zeigt die Gasentnahme, die entweder zum Brenner Motor geführt wird.Point 21 shows the gas extraction that either led to the burner motor will.

Claims (7)

P a t e n t a n s p r ü c h e 1.. Anlage zur Herstellung von Methangas aus Biomasse zum Betrieb eis Verbrennungsmotors, oder eines Gasbrenners, dadurch gekennzeichnet, daß die Biomasse, sowohl Gülle als auch Festmist sein kann und bis zur Pumpfähigkeit homogenisiert wird. P a t e n t a n s p r ü c h e 1 .. Plant for the production of methane gas from biomass to operate an internal combustion engine, or a gas burner, thereby characterized that the biomass, both manure and solid manure can be and up to is homogenized for pumpability. 2. Nach Anspruch 1, d a d u r c h g e k e n n z e i c h n e t, daß der Großbehälter in 3 bzw. 4 Behälterteile aufgeteilt ist und zwar übereinanderliegend.2. According to claim 1, d a d u r c h g e k e n n z e i c h n e t that the large container is divided into 3 or 4 container parts, one on top of the other. 3. Nach Anspruch 1 und 2, dadurch gekennzeichnet, daß die Biomasse nicht nur über einen Wärmetauscher erwärmt wird, sondern mit warmen oder heißem Wasser.3. According to claim 1 and 2, characterized in that the biomass is not only heated via a heat exchanger, but with warm or hot Water. 4. Nach Anpruch- 1, 2, u. 3, dadurch gekennzeichnet, daß der Gärbehälterinhalt bei Temperaturverlust nicht nur über einen '!ärmetauscher wieder aufgewärmt wird, sondern mit zugeführtem warmen oder heißem Wasser.4. According to claim 1, 2, and 3, characterized in that the fermentation tank content in the event of a loss of temperature, it is not only reheated via an '! heat exchanger, but with added warm or hot water. 5. Nach Anspruch 1, 2, 3, und 4, dadurch gekennzeichnet, daß nicht die volle tcisliche Biomasse in den Gärbehälter gegeben lrd, sondern nur 2/3 oder 3/4. Das restliche 1/3 oder 1/4 wird zur Ausgleichung der Temperaturverluste, die innerhalb von 24 Stunden auftreten, genommen.5. According to claim 1, 2, 3, and 4, characterized in that not the full tcisliche biomass in the fermentation tank lrd, but only 2/3 or 3/4. The remaining 1/3 or 1/4 is used to compensate for the temperature losses that occur within 24 hours. 6. Nach Anspruch 1, 2, 3, 4 und 5, dadruch gekennzeichnet.6. According to claim 1, 2, 3, 4 and 5, characterized thereby. daß bei Gärtemperaturen wischen 540 C bis 67° C aus dem ausgefaulten Gut Wärmerückgewinnung vorgenommen werden kann, that at fermentation temperatures between 540 C to 67 ° C from the rotten Good heat recovery can be made 7. Nach Anspruch 1, 2, 3, 4, 5 und 6, d a d u r c h g e k e n n z e i c hnet, daß die Anlage automatisch sowohl per Hand gesteuert werden kann.7. According to claim 1, 2, 3, 4, 5 and 6, it is indicated that the system can be operated automatically by both Can be hand controlled.
DE19792931380 1979-06-16 1979-08-02 Farmyard manure gas generator - combining antechamber, fermentation and sealing tank in one compact unit Ceased DE2931380A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
DE19792924387 DE2924387A1 (en) 1979-06-16 1979-06-16 PLANT WITH DEVICE FOR PRODUCING METHANE GAS FROM ORGANIC RESIDUES
DE19792931380 DE2931380A1 (en) 1979-06-16 1979-08-02 Farmyard manure gas generator - combining antechamber, fermentation and sealing tank in one compact unit

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19792924387 DE2924387A1 (en) 1979-06-16 1979-06-16 PLANT WITH DEVICE FOR PRODUCING METHANE GAS FROM ORGANIC RESIDUES
DE19792931380 DE2931380A1 (en) 1979-06-16 1979-08-02 Farmyard manure gas generator - combining antechamber, fermentation and sealing tank in one compact unit

Publications (1)

Publication Number Publication Date
DE2931380A1 true DE2931380A1 (en) 1981-02-26

Family

ID=39940658

Family Applications (2)

Application Number Title Priority Date Filing Date
DE19792924387 Withdrawn DE2924387A1 (en) 1979-06-16 1979-06-16 PLANT WITH DEVICE FOR PRODUCING METHANE GAS FROM ORGANIC RESIDUES
DE19792931380 Ceased DE2931380A1 (en) 1979-06-16 1979-08-02 Farmyard manure gas generator - combining antechamber, fermentation and sealing tank in one compact unit

Family Applications Before (1)

Application Number Title Priority Date Filing Date
DE19792924387 Withdrawn DE2924387A1 (en) 1979-06-16 1979-06-16 PLANT WITH DEVICE FOR PRODUCING METHANE GAS FROM ORGANIC RESIDUES

Country Status (1)

Country Link
DE (2) DE2924387A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2580294A1 (en) * 1985-04-16 1986-10-17 Sgn Soc Gen Tech Nouvelle Fermentation process and improvement to packed fermenters.
CN106881333A (en) * 2017-03-03 2017-06-23 成都冠禹科技有限公司 A kind of multipurpose organic garbage biochemical treating device based on new energy

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3138452A1 (en) * 1981-09-23 1983-06-09 Rüdiger 5563 Kröv Mergen Device for treating biomass to recover methane gas
DE3602860A1 (en) * 1986-01-31 1987-08-20 Gav Ges Fuer Anaerobe Verfahre Process for fermenting organic waste materials
CH682746A5 (en) * 1990-09-18 1993-11-15 Walter Schmid A method and system for recycling of organic matter.
CH688476A5 (en) * 1993-04-21 1997-10-15 Walter Schmid Method for controlling a Vergaerungsanlage.
CH685494A5 (en) * 1993-09-08 1995-07-31 Buehler Ag Process and plant for the fermentation of organic waste.

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2580294A1 (en) * 1985-04-16 1986-10-17 Sgn Soc Gen Tech Nouvelle Fermentation process and improvement to packed fermenters.
CN106881333A (en) * 2017-03-03 2017-06-23 成都冠禹科技有限公司 A kind of multipurpose organic garbage biochemical treating device based on new energy
CN106881333B (en) * 2017-03-03 2019-04-05 南京灵雀智能制造有限公司 A kind of multipurpose organic garbage biochemical treating device based on new energy

Also Published As

Publication number Publication date
DE2924387A1 (en) 1981-01-08

Similar Documents

Publication Publication Date Title
WO1982000299A1 (en) Plant for the production of fuel gas by anaerobic fermentation of organic materials
DE2931380A1 (en) Farmyard manure gas generator - combining antechamber, fermentation and sealing tank in one compact unit
DE3138452A1 (en) Device for treating biomass to recover methane gas
WO1984000038A1 (en) Process and plant for producing biogas
EP0179234B1 (en) Process and apparatus for the treatment of sewage sludge
DE2934680A1 (en) Methane gas prodn. - from organic residual substances using hot liq. in closed circuit
DE3305624A1 (en) Device for the production of biogas from liquid manure
DE69607596T2 (en) METHOD AND DEVICE FOR PROCESSING WASTE
EP1704221B1 (en) Biogas fermentation installation
DE3117638A1 (en) Process and system for obtaining biogas by methane fermentation
DE3103693A1 (en) Process and apparatus for producing biogas
DE923539C (en) Process for the production of combustible gas by biological means
DE102011008762B4 (en) System for heating drinking water and for killing legionella and other germs in the drinking water
Vamos et al. Ammonia poisoning in carp. 3. The oxygen content as a factor influencing the toxic limit of ammonia
DE3816822A1 (en) Pasteurising apparatus, transportable in a container structure, for the treatment and hygienisation of pasty substrates, such as, for example, liquid manure
DE376697C (en) Method for heating sludge digestion rooms
DE2206245A1 (en) METHOD AND DEVICE FOR HEATING ROOMS AND HEATING A LIQUID MEDIUM
DE588651C (en) Equipment for feeding high pressure vessels
DE3335918A1 (en) Apparatus for the anaerobic treatment of effluents
DE102018122246B4 (en) Energy-efficient system for the production of biogas and fertilizers
DE3304365A1 (en) Process and plant for treating sewage sludge by pasteurisation and subsequent putrefaction
DE2940998A1 (en) METHOD FOR THE PRODUCTION OF METHANE AND A PLANT FOR CARRYING OUT THE METHOD
DE10256014A1 (en) Using pre-used fat and grease as fuel for diesel engines comprises filtration, washing with water, drying and storage under pure nitrogen and subsequent heating
AT96814B (en) Method and apparatus for producing crystallized carbonate of soda.
DE523786C (en) Device for digesting sewage sludge

Legal Events

Date Code Title Description
8127 New person/name/address of the applicant

Owner name: SAUFF, HEINZ, 4000 DUESSELDORF, DE

8131 Rejection