PL436770A1 - Method for digestate dewatering, especially in a biogas plant and a plant for digestate dewatering, especially from a biogas plant - Google Patents

Method for digestate dewatering, especially in a biogas plant and a plant for digestate dewatering, especially from a biogas plant

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Publication number
PL436770A1
PL436770A1 PL436770A PL43677021A PL436770A1 PL 436770 A1 PL436770 A1 PL 436770A1 PL 436770 A PL436770 A PL 436770A PL 43677021 A PL43677021 A PL 43677021A PL 436770 A1 PL436770 A1 PL 436770A1
Authority
PL
Poland
Prior art keywords
digestate
tank
dewatering
dome
biogas plant
Prior art date
Application number
PL436770A
Other languages
Polish (pl)
Other versions
PL245655B1 (en
Inventor
Mirosław Michalak
Jacek DACH
Original Assignee
Dynamic Biogas Spółka Z Ograniczoną Odpowiedzialnością Spółka Komandytowa
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 Dynamic Biogas Spółka Z Ograniczoną Odpowiedzialnością Spółka Komandytowa filed Critical Dynamic Biogas Spółka Z Ograniczoną Odpowiedzialnością Spółka Komandytowa
Priority to PL436770A priority Critical patent/PL245655B1/en
Publication of PL436770A1 publication Critical patent/PL436770A1/en
Publication of PL245655B1 publication Critical patent/PL245655B1/en

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Classifications

    • 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

Landscapes

  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

Przedmiotem zgłoszenia jest sposób odwadniania pofermentu, zwłaszcza w biogazowni oraz instalacja do odwadniania pofermentu, zwłaszcza z biogazowni. W sposobie odwadniania pofermentu otrzymany ze zbiornika fermentacyjnego biogazowni (1) poferment o stopniu uwodnienia poniżej 97% transportuje się do zbiornika pofermentu (1), zamkniętego od góry elastyczną kopułą membranową (2), którą wcześniej montuje się pod kopułą zewnętrzną (3) zbiornika pofermentu (1), po czym za pomocą instalacji grzewczej (4) umieszczonej na dnie zbiornika pofermentu (1) poferment podgrzewa się do temperatury fermentacji mezofilnej mieszczącej się w przedziale od 34°C do 44°C. Z systemu medium chłodzącego (5) do przestrzeni między elastyczną kopułą membranową (2) i kopułą zewnętrzną (3) doprowadza się medium chłodzące, którego temperaturę utrzymuje się w granicach od 3°C do 27°C, a następnie spływające po dolnej powierzchni elastycznej kopuły membranowej (2) skropliny z pofermentu odbiera się przez układ odbioru wody (7) wyposażony w system separacyjny (8). Za pomocą systemu separacyjnego (8) wodę ze skroplin oddziela się od gazu i transportuje układem odbioru wody (7) na zewnątrz zbiornika pofermentu (1).The subject of the application is a method of digestate dewatering, especially in a biogas plant, and an installation for digestate dewatering, especially from a biogas plant. In the digestate dewatering method, the digestate obtained from the fermentation tank of the biogas plant (1) with a degree of hydration below 97% is transported to the digestate tank (1), closed at the top with a flexible membrane dome (2), which is previously installed under the outer dome (3) of the digestate tank (1), and then, by means of a heating installation (4) located at the bottom of the digestate tank (1), the digestate is heated to the mesophilic fermentation temperature ranging from 34 ° C to 44 ° C. From the cooling medium system (5), a cooling medium is supplied to the space between the flexible diaphragm dome (2) and the outer dome (3), the temperature of which is kept between 3 ° C and 27 ° C, and then flows down the bottom surface of the flexible dome membrane (2) condensate from the digestate is collected through the water collection system (7) equipped with a separation system (8). The condensate water is separated from the gas by the separation system (8) and transported through the water receiving system (7) outside the digestate tank (1).

PL436770A 2021-01-26 2021-01-26 Method of dewatering digestate, especially in a biogas plant and installation for dewatering digestate, especially from a biogas plant PL245655B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL436770A PL245655B1 (en) 2021-01-26 2021-01-26 Method of dewatering digestate, especially in a biogas plant and installation for dewatering digestate, especially from a biogas plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PL436770A PL245655B1 (en) 2021-01-26 2021-01-26 Method of dewatering digestate, especially in a biogas plant and installation for dewatering digestate, especially from a biogas plant

Publications (2)

Publication Number Publication Date
PL436770A1 true PL436770A1 (en) 2022-08-01
PL245655B1 PL245655B1 (en) 2024-09-16

Family

ID=83721702

Family Applications (1)

Application Number Title Priority Date Filing Date
PL436770A PL245655B1 (en) 2021-01-26 2021-01-26 Method of dewatering digestate, especially in a biogas plant and installation for dewatering digestate, especially from a biogas plant

Country Status (1)

Country Link
PL (1) PL245655B1 (en)

Also Published As

Publication number Publication date
PL245655B1 (en) 2024-09-16

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