[go: up one dir, main page]

WO2012015635A2 - Procédés de fabrication d'huiles de pyrolyse dérivées de biomasse à teneur réduite en acide et de phase stable - Google Patents

Procédés de fabrication d'huiles de pyrolyse dérivées de biomasse à teneur réduite en acide et de phase stable Download PDF

Info

Publication number
WO2012015635A2
WO2012015635A2 PCT/US2011/044595 US2011044595W WO2012015635A2 WO 2012015635 A2 WO2012015635 A2 WO 2012015635A2 US 2011044595 W US2011044595 W US 2011044595W WO 2012015635 A2 WO2012015635 A2 WO 2012015635A2
Authority
WO
WIPO (PCT)
Prior art keywords
biomass
derived pyrolysis
pyrolysis oil
base
mixing
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/US2011/044595
Other languages
English (en)
Other versions
WO2012015635A3 (fr
Inventor
Mark B. Koch
Timothy A. Brandvold
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Honeywell UOP LLC
Original Assignee
UOP LLC
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 UOP LLC filed Critical UOP LLC
Publication of WO2012015635A2 publication Critical patent/WO2012015635A2/fr
Publication of WO2012015635A3 publication Critical patent/WO2012015635A3/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • 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
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock

Definitions

  • the present invention generally relates to methods for producing biofueis, and more particularly relates to methods for producing phase stable, reduced acid biomass- derived pyrolysis oils.
  • Biomass-derived pyrolysis oil can be burned directly as fuel for certain boiler and furnace applications, and can also serve as a potential feedstock in the production of biofueis in petroleum refineries or in stand-alone process units.
  • Biomass-derived pyrolysis oil has the potential to replace up to 60% of transportation fuels, thereby reducing the dependency on conventional petroleum and reducing its environmental impact.
  • biomass-derived pyrolysis oil is a complex, highly oxygenated organic liquid having properties that currently limit its utilization as a fuel/biofuel, particularly for diesel applications.
  • biomass-derived pyrolysis oil has high acidity (with a low pH and high total acid number (TAN)) making it corrosive to storage, pipes, and downstream equipment, with low energy density and susceptibility to increased viscosity over time.
  • Conventional biomass-derived pyrolysis oil typically has a pH of ⁇ 3 and a TAN >150.
  • the high acidity and low energy density of the biomass-derived pyrolysis oil is attributable in large part to oxygenated hydrocarbons in the oil, particularly carboxylic acids such as formic acid, acetic acid, etc.
  • Oxygenated hydrocarbons as used herein are organic compounds containing hydrogen, carbon, and oxygen. The oxygenated hydrocarbons in the oil are derived from oxygenated hydrocarbons in the gaseous pyrolysis products produced during pyrolysis.
  • phase instability results in phase separation, viscosity increases, and often, solids formation. Such phase instability reduces utilization of the biomass-derived pyrolysis oil as a biofuel.
  • phase stable, reduced acidity biomass derived pyrolysis oils it is desirable to provide methods for producing phase stable, reduced acidity biomass derived pyrolysis oils. It is also desirable to produce phase stable, reduced acid biomass-derived pyrolysis oils having increased energy density.
  • a method for producing phase stable, reduced acid biomass-derived pyrolysis oil comprises providing a biomass-derived pyrolysis oil having a determined water content no greater than 30% by weight. A base is mixed with the biomass-derived pyrolysis oil.
  • Methods are provided for producing phase stable, reduced acid biomass-derived pyrolysis oil from water-containing biomass-derived pyrolysis oil, in accordance with yet another exemplary embodiment of the present invention.
  • the method comprises selecting a base comprising either an inorganic base or a nitrogen-containing base. At least a portion of the water is removed from the water-containing biomass-derived pyrolysis oil, the base, or both.
  • the base is added to the water-containing biomass-derived pyrolysis oil to produce reduced acid biomass-derived pyrolysis oil.
  • Methods are provided for producing phase stable, reduced acid biomass-derived pyrolysis oil in accordance with yet another exemplary embodiment of the present invention.
  • the method comprises providing water-containing biomass-derived pyrolysis oil.
  • FIG. 1 is a flow chart of a method for producing phase stable, reduced acid biomass-derived pyrolysis oils, according to exemplary embodiments of the present invention. DETAILED DESCRIPTION
  • a method 10 for producing phase stable, reduced acid biomass-derived pyrolysis oil begins by providing conventional biomass-derived pyrolysis oil from a source such as a feed tank or other source operative to provide such oil (step 100).
  • Biomass-derived pyrolysis oil is available from, for example, Ensyn Technologies Inc., of Ontario, Canada.
  • the composition of biomass-derived pyrolysis oil is somewhat dependent on feedstock and processing variables.
  • the biomass-derived pyrolysis oil may be produced, for example, from fast pyrolysis of wood biomass in a pyrolysis reactor. However, virtually any form of biomass can be considered for pyrolysis to produce biomass-derived pyrolysis oil.
  • biomass- derived pyrolysis oil may alternatively be referred to herein as "water-containing biomass- derived pyrolysis oil.”
  • method 10 continues by selecting a base to neutralize the carboxylic acids in the water-containing biomass-derived pyrolysis oil, thereby reducing the acidity of the water-containing biomass-derived pyrolysis oil (step 200).
  • neutralization is a chemical reaction whereby the acids in the water-containing biomass-derived pyrolysis oil and the selected base react to form water and a salt.
  • solvated hydrogen ions hydroonium ions, H 3 0 +
  • hydroxide ions OH "
  • the base comprises either an inorganic base or a nitrogen-containing base.
  • the inorganic bases are strong bases.
  • a strong base is a basic chemical compound that is able to deprotonate weak acids in an acid-base reaction. Compounds with a pK a of more than 13 are considered strong bases. Very strong bases are even able to deprotonate very weakly acidic C-H groups in the absence of water.
  • Suitable exemplary inorganic bases include metal oxides, metal alkoxides, metal carbonates of the alkali and alkaline earth metals, alkali and alkaline earth exchanged zeolites (e.g., Ca-X zeolite), mixed metal oxides (e.g., hydrotalcite), metal hydroxides, and combinations thereof.
  • Exemplary suitable metal oxides comprise calcium oxide, magnesium oxide, and combinations thereof.
  • Exemplary suitable metal alkoxides comprise sodium ethoxide, potassium tert- butoxide, and combinations thereof.
  • Exemplary suitable metal carbonates comprise potassium carbonate (K 2 CO 3 ), sodium carbonate (Na 2 C0 3 ), and calcium carbonate (CaC0 3 ).
  • Exemplary suitable metal hydroxides comprise lithium hydroxide (LiOH), sodium hydroxide (NaOH), potassium hydroxide ( OH), rubidium hydroxide (RbOH), caesium hydroxide (CsOH), magnesium hydroxide (Mg(OH) 2 ), calcium hydroxide (Ca(OH) 2 ), strontium hydroxide (Sr(OH) 2 ), barium hydroxide (Ba(OH) 2 ), and combinations thereof.
  • the metal hydroxides generate water when neutralizing carboxylic acids, with the essential reaction being the combination of hydrogen ions with hydroxyl ions to form water.
  • the maximum amount of water produced during neutralization with a metal hydroxide comprises 1 mole eq water to 1 mole eq of neutralized acid. The exact amount of the water produced depends on the selected base.
  • the phase stable, reduced acid biomass-derived pyrolysis oil has a water content no greater than 30 weight percent (wt.%).
  • the terms "30 weight percent” and “30% by weight” as used herein means +/- 3 weight percent of 30 weight percent.
  • the water content of the reduced acid biomass-derived pyrolysis oil after the selected base is added to the water-containing biomass-derived pyrolysis oil is determined (the "determined water content") (step 300).
  • the selected base is added to the water-containing biomass-derived pyrolysis oil to produce reduced acid biomass-derived pyrolysis oil.
  • the water content of the reduced acid biomass-derived pyrolysis oil to be produced is determined to be greater than 30 wt.%, at least a portion of the water is removed from the water-containing biomass- derived pyrolysis oil, the base, or both.
  • x the concentration of water in the phase stable, reduced acid biomass-derived pyrolysis oil expressed as g H 2 0/g oil;
  • a the amount of the starting water-containing biomass-derived pyrolysis oil to be treated in grams
  • b the concentration of water in the starting water-containing biomass-derived pyrolysis oil expressed as g H 2 0/g starting oil (as determined by Karl Fischer Reagent Titration Method (ASTM D 1364), as noted previously);
  • c the concentration of carboxylic acids in the starting water-containing biomass- derived pyrolysis oil expressed as mol acid/gram oil (determined by the method as hereinafter described);
  • g amount of water in grams produced by neutralization of the pyrolysis oil acids. This is dependent on the nature of the neutralizing base such that for:
  • the concentration of carboxylic acids in the starting water-containing biomass- derived pyrolysis oil (“c" in equation (I) above), is determined by the following method adapted from Dence, C.W., Determination of carboxyl groups [in lignin], Methods Lignin Chem. (1992), p. 458-464: A solution of 0.05N tetra-n-butylammonium hydroxide solution (TnBAH) is prepared by diluting 50.0 milliliters (mL) of 1.0N TnBAH (Aldrich, SAP# 1014519, lOOmL) solution to 1.00 liters (L) in isopropanol.
  • TnBAH 0.05N tetra-n-butylammonium hydroxide solution
  • the solution is mixed thoroughly before transferring the solution to a Dosimat bottle. lmL of concentrated HC1 is added to lOOmL of deionized water and mixed thoroughly. 4mL of this solution is added to 140mL of DMF ( ⁇ , ⁇ -dimethylformamide) (available from, for example, Burdick & Jackson of Muskegon, MI (USA)) for titration of samples. To standardize the titrant, 0.15-0.20g of dried benzoic acid is weighed into a titration beaker and the weight recorded to the nearest 0.1 mg. 120mL of the DMF solution is added to the benzoic acid and titrated with the TnBAH solution. The standardization should be done in duplicate. The Normality is calculated to three significant figures and the standardization repeated every three hours.
  • the titration beaker is blanketed with nitrogen and stirred for 5 minutes before titration.
  • the selected base is added to the water-containing biomass-derived pyroiysis oil to produce reduced acid biomass-derived pyroiysis oil (step 400).
  • the amount of the selected base (f in equation (I) above and equation (II) below) to be added to the water-containing biomass- derived pyroiysis oil to neutralize the starting carboxylic acid content is determined according to the following equation (II):
  • a the amount of the starting water-containing biomass-derived pyrolysis oil to be treated in grams
  • c the concentration of carboxylic acids in the starting water-containing biomass- derived pyrolysis oil expressed as mol acid/gram oil (as determined above);
  • e the concentration of neutralizing base in mol base/gram as provided by the manufacturer or determined using methods known by those skilled in the art (i.e., dilution of a more concentrated base solution and/or titration against a standard acid).
  • the base is added at an effective rate to maintain the temperature of the mixture at less than 40°C.
  • the base is added at a temperature from 20°C to 40°C.
  • a solid base may be dissolved in an organic solvent (thereby producing a base solution) prior to addition of the base to the water-containing biomass-derived pyrolysis oil.
  • Suitable exemplary organic solvents comprise methanol, ethanol, and combinations thereof.
  • the addition of the solvent ( 40% to 95% by volume) allows the base to be added gradually in a controlled manner, without raising the water content of the resultant phase stable, reduced acid biomass-derived pyrolysis oil above the threshold value.
  • the solvent raises the solubility of the components in the mixture. Less solvent is needed when the water produced in the titration (during neutralization) does not exceed the solubility level of the biomass-derived pyrolysis oil. If an excess of base is added, a precipitate may form that may be removed by filtration.
  • the water content of the reduced acid biomass-derived pyrolysis oil to be produced (“x" in equation (I) above) is determined to be greater than 30 weight percent, at least a portion of the water is removed from the water-containing biomass-derived pyrolysis oil, the base, or both (step 500) prior to addition of the selected base as described above (step 400).
  • Water may be removed from the water-containing biomass-derived pyrolysis oil, the base, or both by methods known to one skilled in the art, for example, distillation, evaporation, or the like.
  • a base may be selected specifically because it does not generate water during the neutralization reaction, for example, the non-hydroxide bases and the nitrogen-containing bases, and therefore little or no water may have to be removed to produce the reduced acid biomass-derived pyrolysis oil with a water content below the threshold value, i.e., a phase stable, reduced acid biomass-derived pyrolysis oil.
  • the water-containing biomass-derived pyrolysis oil has a water content below the threshold value and the selected base does not generate water during neutralization, the removal of water from the reduced acid biomass- derived pyrolysis oil is unnecessary to produce a phase stable, reduced acid biomass- derived pyrolysis oil because the water content thereof has been maintained below the threshold value.
  • the reduced acid biomass-derived pyrolysis oil may be inspected (step 600) to verify that there is no phase separation. Phase separation typically occurs, if at all, within 48 hours after the base is added to the water-containing biomass- derived pyrolysis oil. If phase separation occurs, additional water may be removed from the reduced acid biomass-derived pyrolysis oil (step 700) by methods known to one skilled in the art, for example distillation and evaporation, until no phase separation is observed on inspection.
  • phase stable, reduced acid biomass-derived pyrolysis oil having a water content no greater than 30 wt% is substantially homogenous, with an acidity (as measured by pH) reduced from that of conventional biomass-derived pyrolysis oil.
  • energy density of the phase stable, reduced acid biomass-derived pyrolysis oil is higher than that of conventional biomass-derived pyrolysis oil.
  • the increased pH, phase homogeneity, and higher energy density of the phase stable, reduced acid biomass-derived pyrolysis oil produced in accordance with exemplary embodiments as described herein improve its suitability as a fuel and biofuel.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

L'invention concerne des procédés de fabrication d'huiles de pyrolyse dérivées de biomasse à teneur réduite en acide et de phase stable. Une huile de pyrolyse dérivée de biomasse ayant une teneur en eau déterminée inférieure ou égale à 30 % en poids est décrite. Une base est mélangée avec l'huile de pyrolyse dérivée de biomasse pour fabriquer une huile de pyrolyse dérivée de biomasse à teneur réduite en acide. Une base est choisie parmi une base inorganique ou une base contenant de l'azote.
PCT/US2011/044595 2010-07-28 2011-07-20 Procédés de fabrication d'huiles de pyrolyse dérivées de biomasse à teneur réduite en acide et de phase stable Ceased WO2012015635A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US12/845,519 2010-07-28
US12/845,519 US20120023809A1 (en) 2010-07-28 2010-07-28 Methods for producing phase stable, reduced acid biomass-derived pyrolysis oils

Publications (2)

Publication Number Publication Date
WO2012015635A2 true WO2012015635A2 (fr) 2012-02-02
WO2012015635A3 WO2012015635A3 (fr) 2012-05-24

Family

ID=45525262

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2011/044595 Ceased WO2012015635A2 (fr) 2010-07-28 2011-07-20 Procédés de fabrication d'huiles de pyrolyse dérivées de biomasse à teneur réduite en acide et de phase stable

Country Status (3)

Country Link
US (1) US20120023809A1 (fr)
AR (1) AR082386A1 (fr)
WO (1) WO2012015635A2 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017006031A1 (fr) * 2015-07-08 2017-01-12 Institut National De La Recherche Agronomique Procédé d'obtention d'acides gras a partir de microorganismes

Families Citing this family (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DK3252128T3 (en) 2006-04-03 2019-04-01 Pharmatherm Chemicals Inc THERMAL EXTRACTION PROCEDURE FOR PREPARING A TAX EXTRACT
US20110284359A1 (en) 2010-05-20 2011-11-24 Uop Llc Processes for controlling afterburn in a reheater and for controlling loss of entrained solid particles in combustion product flue gas
US8499702B2 (en) 2010-07-15 2013-08-06 Ensyn Renewables, Inc. Char-handling processes in a pyrolysis system
US8669405B2 (en) * 2011-02-11 2014-03-11 Kior, Inc. Stable bio-oil
US9441887B2 (en) 2011-02-22 2016-09-13 Ensyn Renewables, Inc. Heat removal and recovery in biomass pyrolysis
JP2014524824A (ja) 2011-04-15 2014-09-25 バイオジェニック リージェンツ エルエルシー 高炭素生体試薬の生成のためのシステムおよび装置
US8841495B2 (en) 2011-04-18 2014-09-23 Gas Technology Institute Bubbling bed catalytic hydropyrolysis process utilizing larger catalyst particles and smaller biomass particles featuring an anti-slugging reactor
US9347005B2 (en) 2011-09-13 2016-05-24 Ensyn Renewables, Inc. Methods and apparatuses for rapid thermal processing of carbonaceous material
US10400175B2 (en) 2011-09-22 2019-09-03 Ensyn Renewables, Inc. Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material
US9109177B2 (en) 2011-12-12 2015-08-18 Ensyn Renewables, Inc. Systems and methods for renewable fuel
EP2847127B1 (fr) 2012-05-07 2020-10-14 Carbon Technology Holdings, LLC Procédé de fabrication d'un charbon actif biogène
US9670413B2 (en) 2012-06-28 2017-06-06 Ensyn Renewables, Inc. Methods and apparatuses for thermally converting biomass
FI126048B (en) * 2013-03-08 2016-06-15 Upm Kymmene Corp Process for modifying bio-oil
WO2014210150A1 (fr) 2013-06-26 2014-12-31 Ensyn Renewables, Inc. Systèmes et procédés pour carburant renouvelable
US12350648B2 (en) 2013-10-24 2025-07-08 Carbon Technology Holdings, LLC Methods and apparatus for producing activated carbon from biomass through carbonized ash intermediates
CA2977092C (fr) 2014-02-24 2022-12-13 Biogenic Reagents Ventures, Llc Charbon actif extremement mesoporeux
KR20150139255A (ko) * 2014-06-03 2015-12-11 에스케이하이닉스 주식회사 반도체 장치 및 그 제조방법
US11413601B2 (en) 2014-10-24 2022-08-16 Carbon Technology Holdings, LLC Halogenated activated carbon compositions and methods of making and using same
EP3337966B1 (fr) 2015-08-21 2021-12-15 Ensyn Renewables, Inc. Système de chauffage à biomasse liquide
CN110366448B (zh) 2016-12-29 2023-05-02 安辛可再生能源有限公司 液体生物质的脱金属化
WO2019241463A1 (fr) 2018-06-14 2019-12-19 Carbon Technology Holdings, LLC Compositions de dioxyde de carbone-silicium poreux biogène et leurs procédés de préparation et d'utilisation
EP3907267A1 (fr) * 2020-05-08 2021-11-10 Basf Se Procédé de purification d'une huile de pyrolyse brute provenant de la pyrolyse de déchets plastiques
US20220098700A1 (en) 2020-09-25 2022-03-31 Carbon Technology Holdings, LLC Bio-reduction of metal ores integrated with biomass pyrolysis
AU2022221681A1 (en) 2021-02-18 2023-10-05 Carbon Technology Holdings, LLC Carbon-negative metallurgical products
BR112023022199A2 (pt) 2021-04-27 2023-12-19 Carbon Tech Holdings Llc Composições de biocarbono com carbono fixo otimizado e processos para produzir o mesmo
CN117940534A (zh) 2021-07-09 2024-04-26 卡本科技控股有限责任公司 用于产生具有高固定碳含量和经优化的反应性的生物碳团粒的方法及由其获得的生物碳团粒
AU2022387418A1 (en) * 2021-11-12 2024-06-27 Carbon Technology Holdings, LLC Biocarbon compositions with optimized compositional parameters, and processes for producing the same

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5034498A (en) * 1989-07-19 1991-07-23 Biocarbons Corporation Method and apparatus for producing water-soluble resin and resin product made by that method
US5371212A (en) * 1992-09-04 1994-12-06 Midwest Research Institute Isolation of levoglucosan from pyrolysis oil derived from cellulose
WO2008098036A1 (fr) * 2007-02-06 2008-08-14 North Carolina State University Préparation et récupération d'un produit issu de la thermolyse de matières lignocellulosiques dans des liquides ioniques
US8598378B2 (en) * 2008-03-14 2013-12-03 University Of Hawaii Methods and compositions for extraction and transesterification of biomass components
EP2105486A1 (fr) * 2008-03-25 2009-09-30 KiOR Inc. Faible nombre d'acide bio brut total
CN102057019B (zh) * 2008-04-06 2014-07-02 环球油品公司 来自生物质衍生热解油的燃料和混合燃料成分
US9102877B2 (en) * 2008-11-12 2015-08-11 Sartec Corporation Systems and methods for producing fuels from biomass
US8920609B2 (en) * 2009-10-01 2014-12-30 Philip H. Steele Method of increasing anhydrosugars, pyroligneous fractions and esterified bio-oil
US8524087B2 (en) * 2009-12-23 2013-09-03 Uop Llc Low metal, low water biomass-derived pyrolysis oils and methods for producing the same
US8519203B2 (en) * 2010-02-17 2013-08-27 Uop Llc Low oxygen biomass-derived pyrolysis oils and methods for producing the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017006031A1 (fr) * 2015-07-08 2017-01-12 Institut National De La Recherche Agronomique Procédé d'obtention d'acides gras a partir de microorganismes
FR3038619A1 (fr) * 2015-07-08 2017-01-13 Agronomique Inst Nat Rech Procede d'obtention d'acides gras a partir de microorganismes

Also Published As

Publication number Publication date
AR082386A1 (es) 2012-12-05
US20120023809A1 (en) 2012-02-02
WO2012015635A3 (fr) 2012-05-24

Similar Documents

Publication Publication Date Title
US20120023809A1 (en) Methods for producing phase stable, reduced acid biomass-derived pyrolysis oils
Malolan et al. Green ionic liquids and deep eutectic solvents for desulphurization, denitrification, biomass, biodiesel, bioethanol and hydrogen fuels: a review
Stankovikj et al. Quantification of bio-oil functional groups and evidences of the presence of pyrolytic humins
Jiang et al. Promoting effect of sodium chloride on the solubilization and depolymerization of cellulose from raw biomass materials in water
US7959765B2 (en) Product preparation and recovery from thermolysis of lignocellulosics in ionic liquids
Lin et al. Hydrothermal carbonization of cellulose in aqueous phase of bio-oil: The significant impacts on properties of hydrochar
JP6369873B2 (ja) 精製のためのバイオマス材料の組成物
Persson et al. Wood-derived acid leaching of biomass for enhanced production of sugars and sugar derivatives during pyrolysis: Influence of acidity and treatment time
AU2010341654A1 (en) Low water biomass-derived pyrolysis oil and processes for preparing the same
US9617489B2 (en) Liquid bio-fuels
US20100155304A1 (en) Treatment of hydrocarbons containing acids
Kamel et al. Utilization of Ficus carica leaves as a heterogeneous catalyst for production of biodiesel from waste cooking oil
EP3094708B1 (fr) Bio-combustibles liquides
CN101885677B (zh) 一种高碱性环烷酸钙的制备方法
Chong et al. Esterification and neutralization of bio-oil from palm empty fruit bunch fibre with calcium oxide
AU2013248186A1 (en) Fuel and process for powering a compression ignition engine
Amara et al. Experimental study of the impact of diesel/biodiesel blends oxidation on the fuel injection system
KR101773060B1 (ko) ＣａＸ 제올라이트 촉매를 이용한 바이오오일의 안정화 방법
CN112169243B (zh) 一种有机危险废物的处理方法
TWI655362B (zh) 用於發動壓縮點火引擎的燃料及方法、該燃料之用途、及使用該燃料之發電系統
Neme et al. Pretreatment of Wheat Straw Using Ionic Liquids for Bioethanol Production: A Review
Слюсарский et al. Effect of preparation method of pyrolysis liquid mixed with coal on its ignition and combustion characteristics
WO2025016747A1 (fr) Procédé de production d'huiles htl présentant une stabilité thermique améliorée et une faible teneur inorganique
WO2011009056A1 (fr) Carburants obtenus à partir de bio-huiles miscibles et leur production
Borton Parametric study for triazabicyclodecene catalyzed biofuel using high free fatty acid feedstocks

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 11812951

Country of ref document: EP

Kind code of ref document: A2

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 11812951

Country of ref document: EP

Kind code of ref document: A2