AR061919A1 - A PROCESS TO BECOME BIOMASS IN A HIGH DENSITY ENERGY MILK AND A LOOSE CARBON CONTENT AND A PROCESS IN WHICH A BIOMASS MILK IS FEEDED TO A HYDROGASIFICATION REACTOR - Google Patents

A PROCESS TO BECOME BIOMASS IN A HIGH DENSITY ENERGY MILK AND A LOOSE CARBON CONTENT AND A PROCESS IN WHICH A BIOMASS MILK IS FEEDED TO A HYDROGASIFICATION REACTOR

Info

Publication number
AR061919A1
AR061919A1 ARP070103201A ARP070103201A AR061919A1 AR 061919 A1 AR061919 A1 AR 061919A1 AR P070103201 A ARP070103201 A AR P070103201A AR P070103201 A ARP070103201 A AR P070103201A AR 061919 A1 AR061919 A1 AR 061919A1
Authority
AR
Argentina
Prior art keywords
biomass
milk
carbon content
feeded
high density
Prior art date
Application number
ARP070103201A
Other languages
Spanish (es)
Inventor
Chan Seung Park
Joseph M Norbeck
Andres Aguirre
Original Assignee
Univ California
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 Univ California filed Critical Univ California
Publication of AR061919A1 publication Critical patent/AR061919A1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/326—Coal-water suspensions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/40—Solid fuels essentially based on materials of non-mineral origin
    • C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00—Treating solid fuels to improve their combustion
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00—Treating solid fuels to improve their combustion
    • C10L9/08—Treating solid fuels to improve their combustion by heat treatments, e.g. calcining
    • C10L9/086—Hydrothermal carbonization
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • 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
    • Y02E50/10—Biofuels, e.g. bio-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
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

Un proceso eficiente de energía para convertir biomasa en una lechada con alta densidad de energía y mayor contenido de carbono. El agua y la biomasa se mezclan a una temperatura y bajo una presion mucho más bajas que la usada en los procesos anteriores, pero bajo un gas no oxidativo, lo que permite la obtencion de una lechada estable que contiene hasta 60% de solidos en peso, 20-40% en peso de carbono, en la lechada. La temperatura es nominalmente de aproximadamente 200°C bajo una presion de gas no oxidativa de aproximadamente 150 libras por pulgada cuadrada, condiciones que son substancialmente menos rigurosas que las requeridas por la técnica previa.An energy efficient process to convert biomass into a grout with high energy density and higher carbon content. Water and biomass are mixed at a temperature and under a pressure much lower than that used in the previous processes, but under a non-oxidative gas, which allows obtaining a stable slurry containing up to 60% solids by weight , 20-40% by weight of carbon, in the slurry. The temperature is nominally about 200 ° C under a non-oxidative gas pressure of about 150 pounds per square inch, conditions that are substantially less stringent than those required by the prior art.

ARP070103201A 2006-07-18 2007-07-18 A PROCESS TO BECOME BIOMASS IN A HIGH DENSITY ENERGY MILK AND A LOOSE CARBON CONTENT AND A PROCESS IN WHICH A BIOMASS MILK IS FEEDED TO A HYDROGASIFICATION REACTOR AR061919A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US11/489,299 US20080016770A1 (en) 2006-07-18 2006-07-18 Method for high energy density biomass-water slurry

Publications (1)

Publication Number Publication Date
AR061919A1 true AR061919A1 (en) 2008-10-01

Family

ID=38957310

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP070103201A AR061919A1 (en) 2006-07-18 2007-07-18 A PROCESS TO BECOME BIOMASS IN A HIGH DENSITY ENERGY MILK AND A LOOSE CARBON CONTENT AND A PROCESS IN WHICH A BIOMASS MILK IS FEEDED TO A HYDROGASIFICATION REACTOR

Country Status (11)

Country Link
US (2) US20080016770A1 (en)
EP (1) EP2046679A2 (en)
JP (1) JP2009543690A (en)
CN (1) CN101489916A (en)
AR (1) AR061919A1 (en)
AU (1) AU2007275759B2 (en)
BR (1) BRPI0711671A2 (en)
CA (1) CA2657376A1 (en)
MX (1) MX2009000699A (en)
TW (1) TW200813208A (en)
WO (1) WO2008011001A2 (en)

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US8603430B2 (en) * 2002-02-05 2013-12-10 The Regents Of The University Of California Controlling the synthesis gas composition of a steam methane reformer
US8118894B2 (en) * 2006-07-18 2012-02-21 The Regents Of The University Of California Commingled coal and biomass slurries
US20080021119A1 (en) * 2006-07-18 2008-01-24 Norbeck Joseph M Operation of a steam methane reformer by direct feeding of steam rich producer gas from steam hydro-gasification
US9822309B2 (en) * 2002-02-05 2017-11-21 The Regents Of The University Of California High carbon concentration biomass and biosolids slurry preparation using a hydro-thermal pretreatment
US8303676B1 (en) 2008-02-19 2012-11-06 Proton Power, Inc. Conversion of C-O-H compounds into hydrogen for power or heat generation
US9698439B2 (en) * 2008-02-19 2017-07-04 Proton Power, Inc. Cellulosic biomass processing for hydrogen extraction
JP5320636B2 (en) * 2008-03-27 2013-10-23 国立大学法人静岡大学 Paper sludge-derived water-soluble saccharide production apparatus and paper sludge-derived water-soluble saccharide production method
CN102071038A (en) * 2009-11-20 2011-05-25 田原宇 Microalgae high-pressure continuous tower-type liquefying process
TWI427142B (en) * 2009-11-23 2014-02-21 Antacor Ltd Method and apparatus for the treatment of material and fuel
US9023243B2 (en) 2012-08-27 2015-05-05 Proton Power, Inc. Methods, systems, and devices for synthesis gas recapture
US10005961B2 (en) * 2012-08-28 2018-06-26 Proton Power, Inc. Methods, systems, and devices for continuous liquid fuel production from biomass
ES2457073B1 (en) * 2012-09-19 2015-02-02 Ingelia, S.L. BIOFUEL PRODUCT AND OBTAINING PROCESS
US10245052B2 (en) * 2013-11-27 2019-04-02 Boston Scientific Scimed, Inc. Systems, devices, and methods for tissue extraction
US10563128B2 (en) 2014-01-10 2020-02-18 Proton Power, Inc. Methods for aerosol capture
US9382482B2 (en) 2014-03-05 2016-07-05 Proton Power, Inc. Continuous liquid fuel production methods, systems, and devices
US9890332B2 (en) 2015-03-08 2018-02-13 Proton Power, Inc. Biochar products and production
CN108192670B (en) * 2017-12-20 2020-12-29 南京大学 Biomass waste liquefaction-gasification treatment method and gasification device

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Also Published As

Publication number Publication date
TW200813208A (en) 2008-03-16
AU2007275759B2 (en) 2013-05-23
MX2009000699A (en) 2009-01-30
US20080016752A1 (en) 2008-01-24
AU2007275759A1 (en) 2008-01-24
US20080016770A1 (en) 2008-01-24
CN101489916A (en) 2009-07-22
EP2046679A2 (en) 2009-04-15
CA2657376A1 (en) 2008-01-24
WO2008011001A3 (en) 2008-11-06
BRPI0711671A2 (en) 2011-11-16
JP2009543690A (en) 2009-12-10
WO2008011001A2 (en) 2008-01-24

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