EP2705118A1 - Traitement de la cellulose à l'aide d'un mélange contenant du glycol, du glycérol et de l'acide p-toluène sulfonique - Google Patents

Traitement de la cellulose à l'aide d'un mélange contenant du glycol, du glycérol et de l'acide p-toluène sulfonique

Info

Publication number
EP2705118A1
EP2705118A1 EP12719282.1A EP12719282A EP2705118A1 EP 2705118 A1 EP2705118 A1 EP 2705118A1 EP 12719282 A EP12719282 A EP 12719282A EP 2705118 A1 EP2705118 A1 EP 2705118A1
Authority
EP
European Patent Office
Prior art keywords
glycerol
diethylene glycol
mixture
starting material
wood
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.)
Withdrawn
Application number
EP12719282.1A
Other languages
German (de)
English (en)
Inventor
Matjaz Kunaver
Natasa Cuk
Edita Jasiukaityte
Frenk Kovac
Samuel Rodman OPRESNIK
Tomaz Katrasnik
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.)
Center of Excellence Polymer Materials and Technologies (Polimat)
GGP Gozdno Gospodarstvo Postojna d o o
Kemijski Institut
Original Assignee
Center of Excellence Polymer Materials and Technologies (Polimat)
GGP Gozdno Gospodarstvo Postojna d o o
Kemijski Institut
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 Center of Excellence Polymer Materials and Technologies (Polimat), GGP Gozdno Gospodarstvo Postojna d o o, Kemijski Institut filed Critical Center of Excellence Polymer Materials and Technologies (Polimat)
Priority to EP12719282.1A priority Critical patent/EP2705118A1/fr
Publication of EP2705118A1 publication Critical patent/EP2705118A1/fr
Withdrawn legal-status Critical Current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, 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
    • C10L1/02—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
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/002—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1011—Biomass
    • C10G2300/1014—Biomass of vegetal origin
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/44—Solvents
    • 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 relates to a method for the production of liquefied cellulose-containing material, such as liquefied wood, wherein the liquefied product is suitable for use as fuel for combustion engines.
  • SI 21884 Liquefaction of wood with the use of the microwaves as a energy source.
  • SI 21883 A method for the liquefaction of wood and wood wastes with polyols and acids.
  • SI 21882 A method for the synthesis of the polyester based on the liquefied wood for the polyurethane foam production.
  • SI 22448 Preparation and utilization of the liquefied wood for the production of the heating energy.
  • SI 21884 describes the fast liquefaction of wood but due to the utilization of the microwaves it is too energy demanding.
  • SI 21883 describes different procedures for the liquefaction of wood but these have yields of less than 64% and a reaction time 3 hours and more.
  • SI 22448 describes the use of the liquefied wood for the production of the heating energy but does not mention the use as fuel for combustion engines .
  • Jasiukaityte et al . (2010, Lignin behavior during wood liquefaction - Characterization by quantitative 31 P, C NMR and size-exclusion chromatography, Catalysis Today, 156: 23-30) describe a method of liquefaction of wood, which method employs a solvent mixture including a large amount of glycerol. The liquefied composition so obtained shows unsatisfactory mechanical properties.
  • WO 2010/069582 WO 2009/115075, WO 2008/105618 and Zhu et al . (2006, Dissolution of cellulose with ionic liquids and its application: a mini -review. Green Chem, 8:325-327) describe various methods for the liquefaction of cellulose-containing solids.
  • the resulting liquids are not equally suitable for use as a fuel for combustion engines, specifically in Diesel engines, as compared with the biofuels of the current invention.
  • the inventors of the present invention have found that the prior art bio-fuels from the liquefaction of wood, e.g., the bio-fuels obtained by the method of Jasiukaityte et al . (ibid.) , are not ideal when used as fuel for combustion engines, because the resulting products have, e.g., a relatively high viscosity.
  • the inventors have found that the high viscosity is a disadvantageous property, which renders the liquefied wood compositions unsuitable for most modern combustion engines .
  • the present invention is based on the unexpected finding that a fuel composition particularly suitable for use for combustion engines, such as Diesel engines, can be obtained from natural resources by liquefaction of cellulose-containing particles in a specific mixture of diethylene glycol, glycerol and p-toluenesulfonic acid, said mixture including a relatively large amount of diethylene glycol .
  • the inventive method does not include a fermentiation step.
  • the present invention thus relates to a method for the production of a liquid fuel from a cellulose- containing solid starting material, said method comprising contacting said solid starting material with a mixture comprising diethylene glycol, glycerol and p- toluenesulfonic acid (PTSA) , wherein ratio of diethylene glycol to glycerol in said mixture is from 1:1 to 20:1 by weight .
  • PTSA p- toluenesulfonic acid
  • the ratio of diethylene glycol to glycerol in said mixture is from 1:1 to 15:1, even more preferred 1:1 to 10:1 by weight.
  • the ratio of diethylene glycol to glycerol in said mixture is from 2:1 to 20:1, or from 2:1 to 15:1, even more preferred from 2:1 to 10:1 by weight.
  • the inventors have found that such relative amounts of diethylene glycol and glycerol yield bio- fuels having a viscosity which is particularly suitable for the use of the fuel for combustion engines, such as Diesel engines.
  • the amount of PTSA in the mixture is from 0.5 %wt (% weight) to 10 %wt, more preferably 1 to 8 %wt , more preferably 2 to 5 %wt, more preferably 2 to 4 %wt, of the sum of weights of diethylene glycol and glycerol in the mixture.
  • PTSA serves as a catalyst for the dissolution of cellulose, hence, as a chemical enhancer of the dissolution process.
  • Fuel products of the present invention preferably have a viscosity at 20°C of between 0.5 and 10 Pa.s, more preferably of between 1 to 8 Pa.s, most preferably of 1.5 to 5 Pa.s.
  • the fuel products have a viscosity at 120°C of between 10-400 mPa.s, more preferably 20-200 mPa.s, most preferably 40- 150 mPa.s.
  • the ratio of the weight of the cellulose-containing starting material to the sum of weights of diethylene glycol and glycerol is from 1:0.5 to 1:10, or 1:1 to 1:10, more preferably 1:1 to 1:6, most preferably 1:2 to 1:4 by weight .
  • said solid starting material comprises at least one component selected from the group consisting of lignocellulosic material, wood, wood sawdust, wood chips, straw, hay, plant fibers, cellulose fibers, cotton fibers, bagasse, and waste materials from a lignin, a tannin or a furfural alcohol production process.
  • a preferred starting material is lignocellulosic material, such as wood chips or wood sawdust .
  • more than 90 %wt, preferably more than 95 %wt, most preferred more than 99 %wt of the particles have a particle size of less than 10 mm, 5 mm, 4 mm, or most preferred less than 2 mm.
  • the particle size shall be understood as being the distance along the longest dimension of the particle.
  • the solid starting material comprises or consists of milled wood. Accordingly, the method may comprise a step of grinding the starting material to a suitable particle size of the invention, prior to the step of contacting the starting material with the mixture comprising diethylene glycol and glycerol .
  • said contacting is at a temperature of above 80°C, preferably at 80- 350°C, 100-250°C, 130-190°C, most preferred 150-180°C.
  • a higher reaction temperature results in faster dissolution of the cellulose-containing starting material.
  • Using the appropriate reaction temperature is advantageous to obtain a useful product. With too low reaction temperature, the reaction may not proceed at the appropriate reaction rate. With too high a temperature the reaction product may become a glue- like or rubberlike substance.
  • the contacting is at atmospheric pressure. In other preferred embodiments the contacting is at 50-1000 kPa (0.5-10 bar), 100-500 kPa (1-5 bar) , most preferably at 100-200 kPa (1-2 bar) .
  • said contacting is for a time period of between 0.5 and 10 hours, more preferably 0.8-7 hours, or 1-5 hours, most preferred 1.5 to 2 hours.
  • said solid starting material and said mixture are blended with a blending device, such as a mixer.
  • the method further comprises a filtration step for removing particles larger than 1, 2, 4, 8, or 16 ⁇ from said fuel after said contacting step.
  • the methods of the invention do not include a fermentation step.
  • preferred products of the invention comprise less than 10 %wt, or 1 %wt, or 0.1 %wt ethanol, or most preferred no ethanol (or no detectable amounts of ethanol) .
  • the invention also relates to a method for the liquefaction of cellulose-containing starting material of the above defined kind.
  • the invention relates to a method of dissolution of cellulose of the above defined kind.
  • the invention relates to the use of a mixture comprising diethylene glycol and glycerol for the liquefaction of cellulose-containing solid material.
  • the invention further relates to the use of the products obtained by methods of the current invention as fuel for a combustion engine.
  • the invention also relates to a liquid fuel produced by a method of the invention.
  • Cellulose in accordance with the present invention, shall be understood to relate to an organic compound with the formula (C G H 10 05) n , in particular to a polysaccharide consisting of a linear chain of a plurality (e.g., more than 100, or more than 1000) 3(1 ⁇ 4) linked D-glucose units.
  • a “combustion engine”, according to the present invention, is any type of engine using the oxidation of fuel as the source of energy.
  • Combustion engines of the invention may be internal combustion engines or external combustion engines.
  • An internal combustion engine is an engine in which the combustion of a fuel occurs with an oxidizer (usually air) in a combustion chamber to produce the thermal/mechanical energy.
  • An external combustion engine is a heat engine where an (internal) working fluid is heated by combustion of an external source, through the engine wall or through a heat exchanger. The fluid then, by expanding and acting on the mechanism of the engine, produces mechanical energy.
  • Preferred internal combustion engines are two-stroke cycle engines, four- stroke cycle engines, Diesel engines, Atkinson cycle engines, Wankel engines, Brayton cycle engines, gas turbines, jet engines (including turbojet, turbofan, ramjet, Rocket) .
  • Preferred external combustion engines are organic Rankine cycle engines, steam engines, Stirling engines.
  • Particularly preferred engines in the context of the present invention are Diesel engines. Further preferred engines are turbine engines.
  • Fiber shall be understood as being any material that stores chemical energy which can later be converted to thermal energy to perform mechanical work in a controlled manner.
  • “Liquefaction”, according to the present invention shall be understood as being the process of dissolving a solid material in a liquid material, the solvent.
  • P-toluenesulfonic acid (4 -methylbenzenesulfonic acid, PTSA)
  • PTSA -methylbenzenesulfonic acid
  • Frermentation within the context of the present invention, shall be understood as being the process of converting sugars, such as mono-saccharides or disaccharides, into ethanol by the action of microorganisms, e.g., yeast.
  • the method for the liquefaction of solid renewable resources utilizes wood, sawdust or other cellulose-containing materials, e.g., cellulose, cotton, waste materials from lignin, tannin or furfural alcohol -production processes.
  • wood, sawdust or other cellulose-containing materials e.g., cellulose, cotton, waste materials from lignin, tannin or furfural alcohol -production processes.
  • the present invention uses a mixture of the diethylene glycol and glycerol, preferably in a ratio that yields a product with appropriate viscosity and particle size.
  • the particle size of the particles in the resulting fuel is below 2 ⁇ .
  • An advantageous property of the methods of the invention is that by changing the ratio between the diethylene glycol and glycerol, the viscosity of the liquefied solid material can be adjusted to be suitable for use as a fuel in specific combustion engines.
  • the production of liquefied cellulose-containing material preferably takes place in an inert reaction vessel, preferably with the aid of a mixer.
  • the invention thus relates to a chemical reaction process of the liquefaction of renewable resources to the product with particles size of preferably less than 2 ⁇ and a viscosity, adopted for the use as a fuel for combustion engines.
  • the invention uses a mixture of the diethylene glycol and glycerol for the liquefaction of renewable resources in a ratio that gives a product with a viscosity and a particle size according to the demands for combustion engine fuels.
  • the viscosity variation can be achieved by changing the ratio between the diethylene glycol and glycerol . With higher loading of diethylene glycol the viscosity is reduced.
  • Such products can then be used as a fuel in the piston engines and internal combustion turbine engines.
  • the liquefied products with higher viscosity can be used as a fuel in external combustion engines, e.g., in engines with higher tolerance to low fuel quality.
  • the invention relates to a process for the liquefaction of wood, wood wastes and similar materials in a mixture of diethylene glycol and glycerin in a ratio that enables the production of a liquid fuel product with viscosity and particles size according to the demands for fuels for combustion engines.
  • the fuel product of the invention is for the replacement of materials produced from crude oil .
  • An important property of the fuel product of the invention is a high energy value fuel for combustion engines. The product reduces the carbon dioxide emission from fossil fuels.
  • the invention presents a chemical reaction process of liquefaction of renewable resources.
  • the liquefaction reaction takes place at elevated temperatures and in the presence of a mixture of diethylene glycol and glycerol . 3 %wt of p-toluenesulfonic acid (relative to the total diethylene glycol and glycerol content) is added.
  • the reaction preferably takes place at temperatures between 150°C and 180°C in a closed reactor vessel made from inert materials, preferably with internal mixing and preferably also with attached condenser for the waste vapor removal .
  • Renewable resources usable according to the invention are wood, wood wastes and or similar materials, such as cellulose, cotton, waste materials from the production of lignin, tannin and furfural alcohol .
  • the solid materials are preferably milled to particles of less than, e.g., 10 mm or 5 mm in size (i.e., largest dimension of the particle) . Smaller particles give higher yields in a shorter reaction time. All ingredients are put into the reactor. The mixture is preferably mixing and heated to temperatures between 150°C and 180°C. The volatile side products of the reaction can be collected by using a condenser. Side products are water, small amounts of acetic acid and furfural. The reaction preferably takes 1.5 to 2 hours. Particles larger than 2 ⁇ can optionally be removed by filtration.
  • the invention relates to a method for the liquefaction of solid renewable resources, such as wood, sawdust, cellulose, cotton, waste materials after production of lignin, tannin and furfural alcohol.
  • the invention lies in the use of a mixture of the diethylene glycol and glycerol in a ratio that yields a product with appropriate viscosity and particle size, e.g., below 2 ⁇ , for use as a fuel in combustion engines.
  • the product can be used as the sole liquid fuel for combustion engines, as a replacement for fuels otherwise produced from crude oils, or it can be used in admixture with such fuels produced from crude oils or mineral oils.
  • EXAMPLE 2 1000 ml reaction vessel with attached mixer and condenser is charged with 100 g of the milled wood, 300 g of a mixture of diethylene glycol : glycerol at a ratio of 4:1 by weight. 9 g of p- toluenesulfonic acid is also added. The mixture is heated to 160 °C to 180 °C under the constant stirring. After 2 hours the product is cooled to room temperature and viscosity and particles size determined. Viscosity at 20°C is 2.3 Pa.s and at 120°C is 75 mPa . s . The particles size is below 2 ⁇ .
  • Liquefied wood was prepared substantially as in Example 1, but the weight proportions of diethylene glycol and glycerol were stepwise varied from 100 %wt glycerol to 100 %wt diethylene glycol.
  • the following viscosities of the resulting fuel were obtained (20°C) :
  • the viscosity of glycerol at 20°C was determined to be 1.4 Pa.s and the viscosity of diethylene glycol was 0.036 Pa.s.

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  • 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)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

Cette invention concerne un procédé de production d'un carburant liquide à partir d'un matériau de départ solide contenant de la cellulose, ledit procédé consistant à mettre ledit matériau de départ solide en contact avec un mélange contenant du diéthylène glycol, du glycérol et de l'acide p-toluène sulfonique en des quantités relatives pour obtenir un carburant pouvant être utilisé dans des moteurs à combustion.
EP12719282.1A 2011-05-04 2012-05-04 Traitement de la cellulose à l'aide d'un mélange contenant du glycol, du glycérol et de l'acide p-toluène sulfonique Withdrawn EP2705118A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP12719282.1A EP2705118A1 (fr) 2011-05-04 2012-05-04 Traitement de la cellulose à l'aide d'un mélange contenant du glycol, du glycérol et de l'acide p-toluène sulfonique

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP11003655 2011-05-04
EP12719282.1A EP2705118A1 (fr) 2011-05-04 2012-05-04 Traitement de la cellulose à l'aide d'un mélange contenant du glycol, du glycérol et de l'acide p-toluène sulfonique
PCT/EP2012/001929 WO2012150043A1 (fr) 2011-05-04 2012-05-04 Traitement de la cellulose à l'aide d'un mélange contenant du glycol, du glycérol et de l'acide p-toluène sulfonique

Publications (1)

Publication Number Publication Date
EP2705118A1 true EP2705118A1 (fr) 2014-03-12

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Family Applications (1)

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EP12719282.1A Withdrawn EP2705118A1 (fr) 2011-05-04 2012-05-04 Traitement de la cellulose à l'aide d'un mélange contenant du glycol, du glycérol et de l'acide p-toluène sulfonique

Country Status (2)

Country Link
EP (1) EP2705118A1 (fr)
WO (1) WO2012150043A1 (fr)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PT107143B (pt) 2013-09-05 2020-04-22 Inst Superior Tecnico Colas poliméricas naturais de base aquosa, de dois componentes, obtidas a partir de derivados da cortiça
SI24656A (sl) 2014-03-12 2015-09-30 Kemijski inštitut Metoda za izdelavo nanokristalinične celuloze
PT107942A (pt) * 2014-10-06 2016-04-06 Inst Superior Tecnico Liquefação de materiais e resíduos lignocelulósicos
EP4139374A1 (fr) 2020-04-23 2023-03-01 Woodchem S.A. Procédé de craquage catalytique de déchets solides provenant de l'industrie des dérivés du pin
CN112063351A (zh) * 2020-08-14 2020-12-11 杭州玖合地面新材料有限公司 一种生物基聚氨酯双组分环氧地板胶

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Publication number Priority date Publication date Assignee Title
WO2008105618A1 (fr) 2007-02-26 2008-09-04 Korea Institute Of Industrial Technology Méthode de production de biocarburant, à l'aide d'algues marines,
DE102008014735A1 (de) 2008-03-18 2009-09-24 Studiengesellschaft Kohle Mbh Verfahren zur Depolymerisation von Zellulose
IT1394398B1 (it) * 2008-12-18 2012-06-15 Eni Spa Procedimento per la produzione di zuccheri da biomassa
IT1392390B1 (it) 2008-12-19 2012-03-02 Eni Spa Procedimento per la conversione di metano, contenuto in correnti gassose, in idrocarburi liquidi idrogenati

Non-Patent Citations (1)

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Title
See references of WO2012150043A1 *

Also Published As

Publication number Publication date
WO2012150043A8 (fr) 2013-01-24
WO2012150043A1 (fr) 2012-11-08

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