WO2012109720A1 - Système intégré de recyclage de matières organiques - Google Patents

Système intégré de recyclage de matières organiques Download PDF

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Publication number
WO2012109720A1
WO2012109720A1 PCT/BR2012/000040 BR2012000040W WO2012109720A1 WO 2012109720 A1 WO2012109720 A1 WO 2012109720A1 BR 2012000040 W BR2012000040 W BR 2012000040W WO 2012109720 A1 WO2012109720 A1 WO 2012109720A1
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Prior art keywords
organic matter
integrated system
fact
matter recycling
recycling
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English (en)
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Fabricio Segabinazzi SIQUEIRA
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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
    • C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
    • 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
    • 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
    • C12M43/00—Combinations of bioreactors or fermenters with other apparatus
    • 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
    • C12M43/00—Combinations of bioreactors or fermenters with other apparatus
    • C12M43/08—Bioreactors or fermenters combined with devices or plants for production of electricity
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/02—Biological treatment
    • C02F11/04—Anaerobic treatment; Production of methane by such processes
    • 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
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • 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
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/30—Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
    • 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 present invention relates to an integrated system for organic matter recycling. More particularly, it discloses a system that reproduces the natural carbon cycle and provides the production of benefits and/or by-products at each stage of the system, with the recycling of the by-products generated in the previous stages of the system.
  • Organic matter is defined biologically as matter with animal or vegetable origin, and geologically as composts of organic origin found above the surface of the soil.
  • Recycling is the term generally used to designate the re-use of materials as raw materials for new products.
  • organic matter is being utilised in the generation of biogas, a type of gaseous mixture of carbon dioxide (C0 2 ) an methane (CH 4 ), produced naturally in anaerobic environment by the action of microorganisms in organic matter, that is fermented in between determined limits of temperature, humidity and acidity.
  • C0 2 carbon dioxide
  • CH 4 methane
  • biogas generating plants like traditional thermal power stations, emit large quantities of C0 2 to the atmosphere, bringing up questions about global warming.
  • the concentration of C0 2 in the atmosphere was maintained constant between 260 and 280 particles per million (ppm).
  • the concentration of C0 2 in the atmosphere began to increase progressively, and since 2003, the concentration of C0 2 has been increasing at a rate above 2 ppm per year, achieving a total of 390 ppm in 2010.
  • the document DE102007007131 describes a biogas power plant coupled to a bio-reactor containing algae.
  • the document US2008/0166265 describes a plant that generates syngas from sewer and other wastes using a plasma converter.
  • the gas is oxidised to generate energy and the wastes are recycled in the bio-reactor and processed by the plasma converted, closing the cycle.
  • the invention describes an integrated system for organic matter recycling that uses 4 processes in a system that reproduces the carbon's natural cycle - decomposition, combustion, cooling and synthesis.
  • the invention provides an integrated system for organic matter recycling with potential use in the treatment of organic wastes, power generation, carbon sequestration, production of biofuels, fertilizers, oxygen and biomass, soil improvement, heating, water desalination and sewage treatment.
  • the invention provides an integrated system for organic matter recycling that promotes flexibility, efficiency and self-sufficiency, because the residues of each stage can be used as raw materials in other stages or be used as by-products.
  • Figure 1 presents a simplified schematic diagram of the integrated system for organic matter recycling, making evident the inter-relationship between the organic matter decomposition unit (100), the combustion unit (200), the cooling unit (300), and the synthesis unit (400).
  • Figure 2 presents schematic representations of possible configurations for the organic matter decomposition unit (100), where the figure 2A presents a simple configuration, including only the anaerobic digester (110) and reservoirs for biogas ( 11 ) and digestate (112); figure 2B presents a simple configuration, including only the pyrolisis chamber (140); figure 2C presents a configuration that combines anaerobic digester (110), a composting chamber (130) and a pyrolisis chamber (140); figure 2D presents a pyrolisis chamber (140) including bio-oil (152) condensing system (350); figure 2E presents the plasma converter (160).
  • Figure 3 presents schematic representation of possible configurations for the combustion unit (200), being figure 3A the simplest possible configuration, including only the combustion chamber (210); figure 3B presents a combustion chamber (210) integrated to a pyrolisis chamber (140), where both chambers are involved in thermal insulation (220); figure 3C is similar to 3B but including a turbine to use the energy (312) from the pressure of the syngas (161 ) generated in the pyrolisis chamber (140); figure 3D is a variation of figure 3C, adding a condenser (350) to separate bio-oil (152) and an equipment (146) to grind and store the biomass from cellulosic origin (145) before that it is directed to the pyrolisis chamber (140); and figure 3E presents a internal combustion engine (230) type Otto, Atkinson, or similar, coupled to a electric generator (320) and a battery (330).
  • a condenser 350
  • FIG. 3E presents a internal combustion engine (230) type Otto, Atkinson, or similar
  • Figure 4 presents schematic representations of possible configurations for the cooling unit (300), being figure 4A the simplest possible configuration, including only the heat engine (310), representing a Stirling engine or thermoelectric generator, among others; figure 4B presents a heat engine (310) similar to Rankine cycle, where a refrigerant travels through a closed cycled, being vaporized (361 ) and condensed (360) at each cycle; figure AC is similar to the previous figure, with the addition of an electric generator (320) and a battery (330); figure 4D is a variation of figure 4B where the refrigerant is comprised by saline water (342), where in this case the refrigerant is constantly replenished in order to desalinate the largest possible quantity of saline water (342); and figure 4E is a variation of figure 4D, where are present a electric generator (320) and a battery (330).
  • figure 4B presents a heat engine (310) similar to Rankine cycle, where a refrigerant travels through a closed cycled,
  • Figure 5 presents schematic representations of possible configurations for the synthesis unit (400), being figure 5A the simplest possible configuration for the synthesis unit (400), including only the photobioreactor (410); figure 5B presents a system that includes the photobioreactor (410), turbine (311 ) to use the energy of the pressure of the oxygen (0 2 ) (414) and other gases produced, and system for separating and processing hydrocarbons (430), and figure 5C presents a system where the photosynthesis medium is comprised by a greenhouse (440).
  • Figure 6 presents a schematic diagram of the integrated system for organic matter recycling, evidencing the most complete and preferred form of the invention, with double lines representing material transport ducts between different components.
  • the integrated organic matter recycling system that reproduces the natural carbon cycle and provides the production of benefits and/or by-products at each stage of the system, object of the present invention, comprehends a organic matter decomposition unit (100), a combustion unit (200), a cooling unit (300) and a synthesis unit (400).
  • the decomposition unit (100) comprehends an anaerobic digester (110) with a culture of acidogenic and acetogenic bacteria and methanogenic microorganisms.
  • Organic residue (106) are deposited into the anaerobic digester (110), said residue (106) are selected among algae deriving from the synthesis unit (400), biomass (404), manure or organic wastes.
  • the microorganisms present in the digester (110) digest the organic residue, producing biogas (114) and digestate (115).
  • the digestate can be used as fertilizer (132).
  • the anaerobic digester (110) has a reservoir (111 ) in the superior portion to store biogas (114) and a second reservoir (112) at opposite to the feeding point to store digestate (115)
  • the contents of the anaerobic digester (110) must contain termophile microorganisms and be maintained at a temperature between 50°C and 52°C, with heat source (203) received from the combustion unit (200).
  • the organic matter (106) is disposed into the digester (110) through a grinder pump (120).
  • part of the digestate (115) if supplied to a composting chamber (130) containing worms of the species Eisenia foetida, Eisenia Andrei, Eisenia hortensis, Enchytraeus buchholzi or Pontoscolex corethrurus, among others.
  • the composting chamber (130) can also receive biomass (404) to the production of humus (130) and liquid fertilizer (132).
  • the heat source (203) is received from the combustion unit (200).
  • the biomass from cellulosic origin (145) passes through a grinding and storage device (146) before being sent to the pyrolisis chamber (140).
  • the biochar (143) is cooled with refrigerant (304) received from the cooling unit (300) and pulverized in a pulveriser (142).
  • the pulverized biochar (144) is supplied to the composting chamber (130), in order to produce terra preta, a compost with excellent fertilizing qualities and great capacity to recover infertile soils.
  • the syngas (161) generated by the pyrolisis chamber (140) is collected and directed to the combustion chamber (210) in order to contribute with the burning process.
  • a condenser (350) is placed in between the pyrolisis chamber (140) gas exhaust and the combustion chamber (210) in order to condense bio-oil (152), stored in a recipient (151 ).
  • the condenser (350) is cooled by refrigerant (304) of the cooling unit (300).
  • the condenser (350) must maintain a minimum temperature above 100°C in order to avoid condensing water.
  • the anaerobic digester (110) can be replaced or work in parallel with a chamber containing organic wastes (106) and a plasma converter (160) that will convert organic matter (106) into syngas (161 ) and a small proportion (approximately 20% in weight, or 5% in volume) of inorganic by-products, known as slag (162), that has many applications, such as construction material (bricks, gravel, sand, concrete additive, thermal insulation), depending on the way it is processed.
  • slag (162) inorganic by-products
  • turbines (311 ) are placed in the gas exhaust of each of the different decomposition systems (110, 140, 160) in order to capture the gas' pressure energy.
  • the gases (114, 161 ) generated in the decomposition unit (100) are used to feed the combustion unit (200).
  • the combustion unit (200) has a combustion chamber (210) with heat source (203) feed by fuel (231 ) and oxygen (414).
  • the fuel (231 ) us comprised by the gases (114, 161 ) generated in the decomposition unit (100).
  • the combustion unit (200) includes a valve ( 16) in the gas inlet that regulates the quantities of gas coming from the different decomposition systems (110, 140, 160) that will be directed to the combustion unit (210 and the excess that will be directed to a reservoir or external gas distribution system.
  • a valve ( 16) in the gas inlet that regulates the quantities of gas coming from the different decomposition systems (110, 140, 160) that will be directed to the combustion unit (210 and the excess that will be directed to a reservoir or external gas distribution system.
  • the combustion chamber (210) includes an ignition system (212) fed by the electricity (321 ) generated in the cooling unit (300).
  • the combustion chamber (210) produces heated exhaust gases (215) comprised by nitrogen, water vapour and carbon dioxide.
  • the combustion unit (200) and other points of the system that receive heat (203) of the combustion unit (200) are separated from the external environment by thermally insulating material (220) in order to avoid unnecessary heat losses.
  • check valve (214) or a compressor is placed in the oxygen inlet (414) in order to avoid the gas leaks.
  • the cooling unit (300) comprehends a heat engine (310) like Stirling engines, steam engines, thermoelectric generators, among others, with heat source (203) comprised by the heated exhaust gas (215) received from the combustion unit (200) and cold sink comprised by refrigerant (304).
  • heat engine like Stirling engines, steam engines, thermoelectric generators, among others, with heat source (203) comprised by the heated exhaust gas (215) received from the combustion unit (200) and cold sink comprised by refrigerant (304).
  • a boiler or evaporator transfers the thermal energy stored in the exhaust gas (215) to the refrigerant (304), heated said refrigerant (304) progressively to a temperature above its boiling point (345) , at the same time that the exhaust gas is progressively cooled (348).
  • the refrigerant in gaseous phase (361 ) then passes through a condenser (350), having its temperature reduced and consequently reverting to the liquid phase (360).
  • the refrigerant substance (304) is comprised by cold saline water (342).
  • the cold saline water (342) Before entering into the system, the cold saline water (342) must be free of solids and impurities, being stored in a specific tank (341 ).
  • the water In the heat engine (310), the water is heated (351 ), distilled (349) and stored in a specific reservoir (347), and the salt (353) is stored in another specific reservoir (343).
  • thermoelectric generator If a thermoelectric generator is used as heat engine (310), the temperature difference between the heat source (203) and the cold sink (304) will be converted directly in electricity (321 ). In other cases, said temperature difference will be converted by the heat engine (310) in mechanic energy (312). An electric generator (320) converts the said mechanic energy (312) in electricity (321 ).
  • the electricity (321 ) generated in the system is stored in a battery (330).
  • the battery (330) can be connected to the public electric energy supply (331 ) both to provide energy (when the system is producing excess energy) and to receive energy (when the system needs external energy).
  • the temperature of the cooled exhaust gas (348) is close to the external environment's temperature.
  • a collecting device (354) recover the condensed liquids (355), preventing these liquids from impairing the proper functioning of the system.
  • combustion unit (200) and the cooling unit (300) can be replaced by an internal combustion engine (230) using the cycles Otto, Atkinson or similar, coupled to an electric generator (320) and a radiator or equivalent for the cooling operation.
  • the synthesis unit (400) comprehends a photobioreactor (410) or any other natural photosynthesis environment, exposed to a light source (412), preferably sunlight, and fed with carbon dioxide, water, fertilizers (132) and nutrients (105) as needed, to produce biomass (404) and emit of oxygen (414).
  • artificial lighting can be supplied for continuing functioning during night time.
  • a turbine (311 ) that converts the difference in the gas pressure between the external and internal environment in mechanical energy (312).
  • water, fertilizer (132) and nutrients (105) be sterilized before being added to the photobioreactor (410).
  • fertilizer (132) be pumped to the photobioreactor (410) by a grinder pump (120).
  • the carbon dioxide added to the photobioreactor (410) is part of the exhaust gas (348) produced by the combustion chamber (210), and cooled by the heat engine (310).
  • the photobioreactor (410) has photosynthetic organisms (431), such as macro algae, microalgae, cyanobacteria, among others.
  • the organisms (431) produced in the photobioreactor (410) are collected and separated from the aqueous environment. It is preferred that the hydrocarbons (434) present in the composition of the organisms (431) are separated, refined and transesterified in processing equipment (430) and later stored in reservoirs (432).
  • the remaining biomass (404) can be recycled in the anaerobic digester (110).
  • the photobioreactor (410) can work in parallel or be replaced by a greenhouse (440) for the production of hydrocarbons (434) and biomass (404) through the cultivation of plants.
  • the system generates products such as humus (131), fertilizer, biochar (143), biogas (114), syngas (161), mechanical energy (312), electricity (321 ), heating (203), salt (353), desalinated water (349), oxygen (414), biomass (404) and hydrocarbons (434).
  • products such as humus (131), fertilizer, biochar (143), biogas (114), syngas (161), mechanical energy (312), electricity (321 ), heating (203), salt (353), desalinated water (349), oxygen (414), biomass (404) and hydrocarbons (434).

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  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Zoology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Wood Science & Technology (AREA)
  • Molecular Biology (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • Genetics & Genomics (AREA)
  • Biomedical Technology (AREA)
  • Sustainable Development (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

L'invention concerne un système intégré de recyclage de matières organiques qui reproduit le cycle naturel du carbone et présente des avantages et/ou crée des sous-produits à chaque étage du système. Ledit système comprend une unité de décomposition de matières organiques (100) avec un digesteur anaérobie (110) contenant une culture de bactéries acidogènes et acétogènes ainsi que des microorganismes méthanogènes permettant de produire du biogaz (114) et un digestat (115), une unité de combustion (200) qui comprend une chambre de combustion (210), une unité de refroidissement (300) qui comprend un moteur thermique (310) avec une source de chaleur (203) constituée du gaz d'échappement chauffé (215) reçu de l'unité de combustion (200) et d'un dissipateur thermique comprenant une substance réfrigérante (304), et une unité de synthèse (400) qui comprend un photobioréacteur (410) ou tout autre environnement de photosynthèse naturelle permettant de produire de l'oxygène (414), de la biomasse (404) et des hydrocarbures (434).
PCT/BR2012/000040 2011-02-14 2012-02-13 Système intégré de recyclage de matières organiques Ceased WO2012109720A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
BRPI1100460-6A BRPI1100460A2 (pt) 2011-02-14 2011-02-14 sistema integrado para reciclagem de matÉria orgÂnica
BRPI1100460-6 2011-02-14

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WO2012109720A1 true WO2012109720A1 (fr) 2012-08-23

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Cited By (8)

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ITTO20120894A1 (it) * 2012-10-12 2014-04-13 Sea Marconi Technologies Di Vander Tumiatti S A S Procedimento di co-produzione di bioenergia e prodotti da conversione integrata di biomasse e rifiuti urbani
CN105294312A (zh) * 2015-11-30 2016-02-03 高洁 一种利用有机废液制备液体生物肥料的方法
CN106567769A (zh) * 2016-10-31 2017-04-19 浙江大学城市学院 一种基于温差发电技术的车用发动机热管理系统及方法
CN108299120A (zh) * 2017-01-11 2018-07-20 深圳市能迩环保科技实业发展有限公司 一种有机肥的制备方法
US10196569B2 (en) * 2015-06-29 2019-02-05 Tongji University Method and system of treating biomass wastes by biochemistry-thermochemistry multi-point interconnection
CN113154410A (zh) * 2021-03-19 2021-07-23 中国辐射防护研究院 一种车载低放可燃废物焚烧装置及工艺
GB2620621A (en) * 2022-07-14 2024-01-17 Economad Solutions Ltd A system for obtaining energy from organic waste
EP4214181A4 (fr) * 2020-09-21 2024-04-24 Bio N IP Pty Ltd Procédé de traitement de déchets organiques

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US20080050800A1 (en) * 2006-08-23 2008-02-28 Mckeeman Trevor Method and apparatus for a multi-system bioenergy facility
WO2009158028A2 (fr) * 2008-06-26 2009-12-30 Novus Energy Llc Systèmes intégrés permettant de produire du biogaz et du combustible liquide à partir d’algues
US20100105127A1 (en) * 2008-10-24 2010-04-29 Margin Consulting, Llc Systems and methods for generating resources using wastes

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080050800A1 (en) * 2006-08-23 2008-02-28 Mckeeman Trevor Method and apparatus for a multi-system bioenergy facility
WO2009158028A2 (fr) * 2008-06-26 2009-12-30 Novus Energy Llc Systèmes intégrés permettant de produire du biogaz et du combustible liquide à partir d’algues
US20100105127A1 (en) * 2008-10-24 2010-04-29 Margin Consulting, Llc Systems and methods for generating resources using wastes

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITTO20120894A1 (it) * 2012-10-12 2014-04-13 Sea Marconi Technologies Di Vander Tumiatti S A S Procedimento di co-produzione di bioenergia e prodotti da conversione integrata di biomasse e rifiuti urbani
WO2014057102A1 (fr) * 2012-10-12 2014-04-17 Sea Marconi Technologies Di Vander Tumiatti S.A.S. Procédé de co-production de bio-énergie et de produits à partir de la conversion intégrée de biomasses et de déchets urbains
US10196569B2 (en) * 2015-06-29 2019-02-05 Tongji University Method and system of treating biomass wastes by biochemistry-thermochemistry multi-point interconnection
CN105294312A (zh) * 2015-11-30 2016-02-03 高洁 一种利用有机废液制备液体生物肥料的方法
CN106567769A (zh) * 2016-10-31 2017-04-19 浙江大学城市学院 一种基于温差发电技术的车用发动机热管理系统及方法
CN108299120A (zh) * 2017-01-11 2018-07-20 深圳市能迩环保科技实业发展有限公司 一种有机肥的制备方法
EP4214181A4 (fr) * 2020-09-21 2024-04-24 Bio N IP Pty Ltd Procédé de traitement de déchets organiques
CN113154410A (zh) * 2021-03-19 2021-07-23 中国辐射防护研究院 一种车载低放可燃废物焚烧装置及工艺
GB2620621A (en) * 2022-07-14 2024-01-17 Economad Solutions Ltd A system for obtaining energy from organic waste
GB2620621B (en) * 2022-07-14 2024-09-18 Economad Solutions Ltd A system for obtaining energy from organic waste

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