AT400711B - Biogas plant - Google Patents

Biogas plant Download PDF

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Publication number
AT400711B
AT400711B AT0169392A AT169392A AT400711B AT 400711 B AT400711 B AT 400711B AT 0169392 A AT0169392 A AT 0169392A AT 169392 A AT169392 A AT 169392A AT 400711 B AT400711 B AT 400711B
Authority
AT
Austria
Prior art keywords
central tube
support material
biogas plant
reactor
microorganisms
Prior art date
Application number
AT0169392A
Other languages
German (de)
Other versions
ATA169392A (en
Original Assignee
Karlsreiter Herbert
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
Application filed by Karlsreiter Herbert filed Critical Karlsreiter Herbert
Priority to AT0169392A priority Critical patent/AT400711B/en
Priority to AT0050094A priority patent/ATA50094A/en
Publication of ATA169392A publication Critical patent/ATA169392A/en
Application granted granted Critical
Publication of AT400711B publication Critical patent/AT400711B/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • C02F3/2806Anaerobic processes using solid supports for microorganisms
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/04Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M25/00Means for supporting, enclosing or fixing the microorganisms, e.g. immunocoatings
    • C12M25/10Hollow fibers or tubes
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

The invention relates to a biogas plant having a reactor 1 which has a central tube 17 to which is fed the biomass 18. Around the central tube 17 is built up support material 4 for microorganisms and, on the inner walls of the reactor 1, in addition, there is further applied support material 3 for microorganisms. The central tube 17 is formed by support material 4 which has channels 13 which, in the case of the central tube 17 pass through the support material, but in the case of the support material 3 on the inner wall of the reactor 1 are only open towards the interior. <IMAGE>

Description

       

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 ist,In der Ausführungsform gemäss Fig. 1 befindet sich in dem Raum, der von dem   Trägermatenal   4 des Zentralrohres 17 umschlossen ist, eine Rühreinrichtung 9. 



  Diese Rühreinrichtung 9 ist dabei mittig im Zentralrohr 17 angeordnet. 



  In der Ausführungsform gemäss Fig. 2 mündet in den von dem Zentralrohr 17 umschlossenen Innenraum das Rohr 11 einer Mammutpumpe ein. 



  Sowohl die Mammutpumpe als auch die Rühreinrichtung 9 sorgen für eine Bewegung der organischen Substanzen im Reaktor 1. Im Falle der Verwendung einer Rühreinrichtung 9 kann die Strömung, je nach Drehrichtung der Rühreinrichtung 9, bzw. der Drehrichtung des Schneidwerkes 24 der   Rühreinrichtung.   eine Strömung in Richtung des Doppelpfeiles 14 erfolgen. Bei Verwendung einer Mammutpumpe, wie des Fig. 2 zeigt, ist eine Strömung nur in Richtung der Pfeile 21 möglich. In beiden   Fällen wird Jedoch   die organische Substanz durch die   Hohlräume   13 des Trägermaterials 4 bewegt. Gleichzeitig wird durch die im Bodenbereich angeordneten Öffnungen 8 und durch die Öffnung des Zentralrohres 17 an seinem oberen Ende. die organische Substanz gepumpt. 



   Um nun bel Verwendung der Rühreinrichtung 9 einen besseren Gaseintrag in die Biomasse zu erreichen, ist ein Rohr 5 vorgesehen (Fig.   1),   durch welches mit Hilfe des durch das Schneidwerk 24 der Rühreinrichtung erzeugten Unterdruckes, Biogas aus dem Gasraum 23 der Biogasaniage angesaugt und in die organische Substanz Im Innenraum des Zentrairohres 17 gebracht werden kann. 



  

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 In the embodiment according to FIG. 1 there is a stirring device 9 in the space which is enclosed by the carrier material 4 of the central tube 17.



  This stirring device 9 is arranged centrally in the central tube 17.



  In the embodiment according to FIG. 2, the tube 11 of a mammoth pump opens into the interior enclosed by the central tube 17.



  Both the mammoth pump and the stirring device 9 ensure a movement of the organic substances in the reactor 1. If a stirring device 9 is used, the flow can, depending on the direction of rotation of the stirring device 9, or the direction of rotation of the cutting unit 24 of the stirring device. a flow in the direction of the double arrow 14. When using a mammoth pump, as shown in FIG. 2, a flow is only possible in the direction of the arrows 21. In both cases, however, the organic substance is moved through the cavities 13 of the carrier material 4. At the same time, through the openings 8 arranged in the bottom area and through the opening of the central tube 17 at its upper end. pumped the organic matter.



   In order to achieve better gas introduction into the biomass bel using the stirring device 9, a tube 5 is provided (FIG. 1) through which, with the help of the vacuum generated by the cutting device 24 of the stirring device, biogas is sucked out of the gas space 23 of the biogas plant and can be brought into the organic substance in the interior of the central tube 17.



  
    

Claims (4)

Patentansprüche 1. Biogasanlage mit einem Reaktor, dadurch gekennzeichnet, dass der Reaktor (1) ein Zentralrohr (17) aufweist, in welches die Biomasse (18) eingeführt wird, wobei um das Zentralrohr (17) Trägermaterial (4) für Mikroorganismen aufgebaut ist und an den Reaktorinnenwänden zusätzlich Trägermaterial (3) für Mikroorganismen angebracht ist.1. Biogas plant with a reactor, characterized in that the reactor (1) has a central tube (17) into which the biomass (18) is introduced, with support material (4) for microorganisms being built up around the central tube (17) and additional support material (3) for Microorganisms is attached. 2. Biogasanlage nach Anspruch 1, dadurch gekennzeichnet, dass das an der Reaktorinnenwand ange- ordnete Trägermaterial (3) Kanäle (13) aufweist, die nach aussen abgeschlossen, nach innen jedoch offen sind. 2. Biogas plant according to claim 1, characterized in that the carrier material (3) arranged on the inner wall of the reactor has channels (13) which are closed to the outside but are open to the inside. 3. Biogasanlage nach Anspruch 1 oder 2, dadurch gekennzeichnet, dass in dem Innenraum, der von dem um das Zentralrohr (17) aufgebaute Trägermatenal (4) umschlossen ist, eine Rühreinrichtung (9) zentral angeordnet ist. 3. Biogas plant according to claim 1 or 2, characterized in that a stirring device (9) is arranged centrally in the interior, which is enclosed by the support material (4) constructed around the central tube (17). 4. Biogasanlage nach Anspruch 1 oder 2. dadurch gekennzeichnet, dass in den Innenraum, der von dem um das Zentralrohr (17) aufgebaute Trägermaterial (4) umschlossen ist, das Rohr (11) einer Mammut- pumpe einmündet. 4. Biogas plant according to claim 1 or 2, characterized in that the tube (11) of a mammoth pump opens into the interior, which is surrounded by the carrier material (4) constructed around the central tube (17).
AT0169392A 1992-08-24 1992-08-24 Biogas plant AT400711B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
AT0169392A AT400711B (en) 1992-08-24 1992-08-24 Biogas plant
AT0050094A ATA50094A (en) 1992-08-24 1994-03-09 BIOGAS PLANT

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT0169392A AT400711B (en) 1992-08-24 1992-08-24 Biogas plant

Publications (2)

Publication Number Publication Date
ATA169392A ATA169392A (en) 1995-07-15
AT400711B true AT400711B (en) 1996-03-25

Family

ID=3518960

Family Applications (1)

Application Number Title Priority Date Filing Date
AT0169392A AT400711B (en) 1992-08-24 1992-08-24 Biogas plant

Country Status (1)

Country Link
AT (1) AT400711B (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT139272B (en) * 1933-08-21 1934-11-10 Max Ing Friedersdorff Biological sewage treatment plant with horizontal flow filter device.
US4683062A (en) * 1984-11-30 1987-07-28 Ceskoslovenska Akademie Ved Method of circulation of a liquid phase through a solid phase particularly for biocatalytical reactions and a device for realization thereof
CH670627A5 (en) * 1986-02-10 1989-06-30 Onoda Alc Kk

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT139272B (en) * 1933-08-21 1934-11-10 Max Ing Friedersdorff Biological sewage treatment plant with horizontal flow filter device.
US4683062A (en) * 1984-11-30 1987-07-28 Ceskoslovenska Akademie Ved Method of circulation of a liquid phase through a solid phase particularly for biocatalytical reactions and a device for realization thereof
CH670627A5 (en) * 1986-02-10 1989-06-30 Onoda Alc Kk

Also Published As

Publication number Publication date
ATA169392A (en) 1995-07-15

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Legal Events

Date Code Title Description
UEP Publication of translation of european patent specification
ELJ Ceased due to non-payment of the annual fee
REN Ceased due to non-payment of the annual fee