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WO2012031622A1 - Method for the acidification of manure - Google Patents

Method for the acidification of manure Download PDF

Info

Publication number
WO2012031622A1
WO2012031622A1 PCT/EP2010/063105 EP2010063105W WO2012031622A1 WO 2012031622 A1 WO2012031622 A1 WO 2012031622A1 EP 2010063105 W EP2010063105 W EP 2010063105W WO 2012031622 A1 WO2012031622 A1 WO 2012031622A1
Authority
WO
WIPO (PCT)
Prior art keywords
manure
acidification
flow
gas
methane
Prior art date
Application number
PCT/EP2010/063105
Other languages
French (fr)
Inventor
Jacob Hendrik Obbo Hazewinkel
Original Assignee
Green Energy Technologies Cv
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 Green Energy Technologies Cv filed Critical Green Energy Technologies Cv
Priority to EP10751932.4A priority Critical patent/EP2613621A1/en
Priority to PCT/EP2010/063105 priority patent/WO2012031622A1/en
Publication of WO2012031622A1 publication Critical patent/WO2012031622A1/en
Priority to US13/784,859 priority patent/US20130186823A1/en

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
    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01C—PLANTING; SOWING; FERTILISING
    • A01C3/00—Treating manure; Manuring
    • 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
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/50—Treatments combining two or more different biological or biochemical treatments, e.g. anaerobic and aerobic treatment or vermicomposting and aerobic treatment
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F3/00—Fertilisers from human or animal excrements, e.g. manure
    • 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
    • C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/02—Odour removal or prevention of malodour
    • 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
    • Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • 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
    • Y02P20/141—Feedstock
    • Y02P20/145—Feedstock the feedstock being materials of biological origin
    • 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

Definitions

  • the invention relates to a method for the acidification of manure .
  • Manure is collected and stored.
  • the pH of manure is
  • acidification has the advantage that more methane is formed in the digestion process by the prevention of the formation of methane by acidification in the storage process, and the advantage that the part of ammonia that would be emitted as a gas is now stored as a nitrogen mineral in the digested manure for use as
  • Nitric acid has been tested and used as an acid. Using nitric acid has the disadvantage of promoting
  • EP 0612704 One method for the acidification of manure is described in EP 0612704.
  • the method comprises adding acid producing bacteria to the manure that are capable to survive in manure by feeding on the substrates in manure.
  • the substrates are converted to acids by mentioned bacteria and provide the reduction of the pH value of manure.
  • a method for the acidification of manure is provided by an acidic flow of an anaerobic digestion device and/or the flow of sulphuric acid from a device that oxidated hydrogen sulfide gas (3 ⁇ 4S) in the biogas from an anaerobic digestion device to sulphuric acid.
  • the major objective of anaerobic digestion of organic material is the production of biogas.
  • organic material for example manure, animal fat or garden waste
  • any acidious flow that can be transported to the manure is to be used as an acid for the acidification of manure for the mentioned purposes.
  • An acidious flow of a digestion device is the flow from the hydrolys phase.
  • the hydrolysis phase is usually, not necessary, the first phase of anaerobic digestion of a mass of organic material.
  • the larger organic molecules, such as proteins, carbohydrates and fats are broken down by microbes to smaller molecules, such as acids.
  • hydrolysis phase has typically, not necessary, a pH ranging from 3 to 5, such as in the digestion device decribed in N2003220 ("Device and method for the anaerobic digestion of organic material to biogas by means of micro-organisms", number 500022935) .
  • Biogas can contain an undisered level of hydrogen sulphur.
  • Hydrogen sulphur (3 ⁇ 4S) causes corrosion to devices such as boilers and engines, when the biogas is used as a fuel.
  • Hydrogen sulphur is oxydized chemically and/or
  • the sulphuric acid has a pH of typically, not necessary, between of 2 to 3.
  • the extra hydrogen sulphide (3 ⁇ 4S) in the biogas can be removed again from the biogas, and chemically and/or biologically oxydized to sulphurous acid, to be used as an acid for the acidification of manure.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Microbiology (AREA)
  • Engineering & Computer Science (AREA)
  • Molecular Biology (AREA)
  • Soil Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Biotechnology (AREA)
  • Biochemistry (AREA)
  • Environmental Sciences (AREA)
  • Fertilizers (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The invention relates to a method for the acidification of manure.By acidifying manure, emissions of methane gas and ammonia gasare prevented significantly. The method for the acidification of manure is provided by an acidic flow of an anaerobic digestion device and/or the flow of sulphuric and/or sulphurous acid from a device that removes hydrogen sulfide gas from biogas from an anaerobic digestion device by chemcial and/or biological oxydation to sulphuric acid. In the case that the manure will be digested, acidification has the advantage that more methane is formed in the digestion process by the prevention of the formation of methane by acidification in the storage process, the advantage that the part of ammonia that would be emitted as a gas is now stored as a nitrogen mineral in the digested manure for use as fertilizer, and the advantage is that the manure has a pH value thatis more preferable for digestion processes in the case the manure will be digested.

Description

METHOD FOR THE ACIDIFICATION OF MANURE
The invention relates to a method for the acidification of manure .
The major objective of the acidification of manure is the suppression of the formation of methane and ammonia gases. Manure is collected and stored. The pH of manure is
typically above 8 and contains biodegradable components. Collected manure therefore will readily become anaerobic and methane gas and ammonia gas is generated and emitted. The emissions of methane gas and ammonia gas must be prevented from an environmental point of view. The emissions of methane gas and ammonia gas are prevented most effectively by maintaining the pH of the manure between not higher than 4.5, preferably between 4 and 4.5. Thus, ammonia is fixed in the water phase as cations and the formation of methane is halted. The pH of the manure is maintained at mentioned values by acidification of the manure. In the case that the manure will be digested, acidification has the advantage that more methane is formed in the digestion process by the prevention of the formation of methane by acidification in the storage process, and the advantage that the part of ammonia that would be emitted as a gas is now stored as a nitrogen mineral in the digested manure for use as
fertilizer .
The acidification of manure by adding acids is common knowledge. Nitric acid has been tested and used as an acid. Using nitric acid has the disadvantage of promoting
denitrification reactions, leading nitrous oxide (N20) gas emissions and loss of valuable fertilizer which causes the pH to increase again. Sulphuric acid has been found as a usefull acid to acidify manure, but will add more sulfur increasing the hydrogen sulphide (¾S) content of the biogas. Organic acids do not have the disadvantage to add extra minerals to mentioned ferilizer that can be undesired. The costs of acidification of manure by adding acid in order to supress the methane and ammonia has prevented wide spread use of this method.
One method for the acidification of manure is described in EP 0612704. The method comprises adding acid producing bacteria to the manure that are capable to survive in manure by feeding on the substrates in manure. The substrates are converted to acids by mentioned bacteria and provide the reduction of the pH value of manure.
It is an object of the present invention to provide an improved method for the acidification of manure.
This and other objects can be achieved by providing a method according to claim 1. A particularly preferred embodiment of the method according to the invention is described in claim 2.
In summary, according to the invention a method for the acidification of manure is provided by an acidic flow of an anaerobic digestion device and/or the flow of sulphuric acid from a device that oxidated hydrogen sulfide gas (¾S) in the biogas from an anaerobic digestion device to sulphuric acid. The major objective of anaerobic digestion of organic material is the production of biogas. In anaerobic
digestion, organic material, for example manure, animal fat or garden waste, is broken down to smaller molecules, such as for instance methane and carbon dioxide, in a number of different stages, substantially in the absense of air or any other source of oxygen. According to the invention any acidious flow that can be transported to the manure is to be used as an acid for the acidification of manure for the mentioned purposes. One example of an acidious flow of a digestion device is the flow from the hydrolys phase. The hydrolysis phase is usually, not necessary, the first phase of anaerobic digestion of a mass of organic material. In hydrolysis, the larger organic molecules, such as proteins, carbohydrates and fats are broken down by microbes to smaller molecules, such as acids. The flow from the
hydrolysis phase has typically, not necessary, a pH ranging from 3 to 5, such as in the digestion device decribed in N2003220 ("Device and method for the anaerobic digestion of organic material to biogas by means of micro-organisms", number 500022935) .
The major product of an anaerobic digestion device is biogas. Biogas can contain an undisered level of hydrogen sulphur. Hydrogen sulphur (¾S) causes corrosion to devices such as boilers and engines, when the biogas is used as a fuel. Hydrogen sulphur is oxydized chemically and/or
biologically to sulphurous oxide, when it is removed from the biogas, forming sulphuric and/or sulphurous acid in a liquid flow. The sulphuric acid has a pH of typically, not necessary, between of 2 to 3. The extra hydrogen sulphide (¾S) in the biogas can be removed again from the biogas, and chemically and/or biologically oxydized to sulphurous acid, to be used as an acid for the acidification of manure.

Claims

Claims
1. Method for the acidification of manure by using acidic transportable flow of an anaerobic digestion device and/or a flow of sulphuric and/or sulphurous acid from a device that removes hydrogen sulphide gas from biogas, said method comprising at least the following steps:
- retrieving from mentioned anaerobic digestion device at least a part of the flow that is in any phase of a digestion process and/or a part of the flow from, and/or retrieving from said device sulphuric and/or sulphurous acid from a device that removes hydrogen sulphide gas from biogas from an anaerobic digestion device by chemical and/or biological oxidation to sulphuric acid,
- transporting said acidic flows to the manure,
in order to significantly reduce emissions of methane gas and ammonia gas, by acidifying the manure.
2. Method according to claim 1,
characterized by
the pH value of said flows being maximum 5.
PCT/EP2010/063105 2010-09-07 2010-09-07 Method for the acidification of manure WO2012031622A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP10751932.4A EP2613621A1 (en) 2010-09-07 2010-09-07 Method for the acidification of manure
PCT/EP2010/063105 WO2012031622A1 (en) 2010-09-07 2010-09-07 Method for the acidification of manure
US13/784,859 US20130186823A1 (en) 2010-09-07 2013-03-05 Method for the acidification of manure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/EP2010/063105 WO2012031622A1 (en) 2010-09-07 2010-09-07 Method for the acidification of manure

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US13/784,859 Continuation US20130186823A1 (en) 2010-09-07 2013-03-05 Method for the acidification of manure

Publications (1)

Publication Number Publication Date
WO2012031622A1 true WO2012031622A1 (en) 2012-03-15

Family

ID=43334400

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2010/063105 WO2012031622A1 (en) 2010-09-07 2010-09-07 Method for the acidification of manure

Country Status (3)

Country Link
US (1) US20130186823A1 (en)
EP (1) EP2613621A1 (en)
WO (1) WO2012031622A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITVR20110230A1 (en) * 2011-12-22 2013-06-23 Aquaser S R L PROCEDURE FOR PROCESSING DIGESTATO
US20150352487A1 (en) * 2014-06-06 2015-12-10 Mark A. Moser Method and Device for Removal of Hydrogen Sulfide from a Gas
US10239016B2 (en) 2016-12-07 2019-03-26 Nuorganics LLC Systems and methods for nitrogen recovery from a gas stream
US10513466B2 (en) 2017-01-16 2019-12-24 Nuorganics LLC System and method for recovering nitrogenous compounds from a gas stream
US20210087089A1 (en) * 2019-09-20 2021-03-25 Pancopia, Inc Animal husbandry nutrient and odor management system
DE102022125827A1 (en) 2022-10-06 2024-04-11 Alzchem Trostberg Gmbh Process for reducing harmful gas emissions from farm manure

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019210998A1 (en) 2018-05-01 2019-11-07 Linde Aktiengesellschaft Method for acidification of manure
WO2022013148A1 (en) * 2020-07-13 2022-01-20 Dsm Ip Assets B.V. Process for the production of biogas

Citations (4)

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GB2013170A (en) * 1977-12-29 1979-08-08 Sweeney J J Anaerobic treatment of waste to produce methane
EP0612704A1 (en) 1992-12-30 1994-08-31 Sta Pro Environment B.V. Process for acidifying manure, in which ammonia is fixed and carbon dioxide gas is emitted
WO2005095009A1 (en) * 2004-03-30 2005-10-13 Nutrient Management Technologies Ltd. Manure treatment process
WO2008131034A2 (en) * 2007-04-16 2008-10-30 Moser Mark A Hydrogen sulfide scrubber

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DE3835468C1 (en) * 1988-10-18 1990-01-25 Gemabau Gesellschaft Fuer Maschinenanlagen Mbh, 2371 Borgstedt, De Process and apparatus for liquid manure treatment
DE4226087A1 (en) * 1992-04-16 1993-10-21 Recycling Energie Abfall Process for the biological processing of organic substances, in particular for anaerobic biological hydrolysis for the subsequent biomethanization and device for carrying out the process
JP3103027B2 (en) * 1995-11-27 2000-10-23 株式会社荏原製作所 Exhaust gas treatment method and apparatus using ammonia in sewage

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2013170A (en) * 1977-12-29 1979-08-08 Sweeney J J Anaerobic treatment of waste to produce methane
EP0612704A1 (en) 1992-12-30 1994-08-31 Sta Pro Environment B.V. Process for acidifying manure, in which ammonia is fixed and carbon dioxide gas is emitted
WO2005095009A1 (en) * 2004-03-30 2005-10-13 Nutrient Management Technologies Ltd. Manure treatment process
WO2008131034A2 (en) * 2007-04-16 2008-10-30 Moser Mark A Hydrogen sulfide scrubber

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP2613621A1

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITVR20110230A1 (en) * 2011-12-22 2013-06-23 Aquaser S R L PROCEDURE FOR PROCESSING DIGESTATO
US20150352487A1 (en) * 2014-06-06 2015-12-10 Mark A. Moser Method and Device for Removal of Hydrogen Sulfide from a Gas
US10239016B2 (en) 2016-12-07 2019-03-26 Nuorganics LLC Systems and methods for nitrogen recovery from a gas stream
US10513466B2 (en) 2017-01-16 2019-12-24 Nuorganics LLC System and method for recovering nitrogenous compounds from a gas stream
US10934223B2 (en) 2017-01-16 2021-03-02 Nuorganics LLC System and method for recovering nitrogenous compounds from a gas stream
US20210087089A1 (en) * 2019-09-20 2021-03-25 Pancopia, Inc Animal husbandry nutrient and odor management system
US12060290B2 (en) * 2019-09-20 2024-08-13 Pancopia, Inc Animal husbandry nutrient and odor management system
DE102022125827A1 (en) 2022-10-06 2024-04-11 Alzchem Trostberg Gmbh Process for reducing harmful gas emissions from farm manure
WO2024074560A1 (en) 2022-10-06 2024-04-11 Alzchem Trostberg Gmbh Method of reducing harmful gas emissions from organic fertilizers

Also Published As

Publication number Publication date
US20130186823A1 (en) 2013-07-25
EP2613621A1 (en) 2013-07-17

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