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WO2009085324A1 - Procédé de production d'acides et esters carboxyliques à chaîne courte à partir de la biomasse et produit obtenu par ce procédé - Google Patents

Procédé de production d'acides et esters carboxyliques à chaîne courte à partir de la biomasse et produit obtenu par ce procédé Download PDF

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Publication number
WO2009085324A1
WO2009085324A1 PCT/US2008/014145 US2008014145W WO2009085324A1 WO 2009085324 A1 WO2009085324 A1 WO 2009085324A1 US 2008014145 W US2008014145 W US 2008014145W WO 2009085324 A1 WO2009085324 A1 WO 2009085324A1
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Prior art keywords
biomass
oil
carboxylic acids
mixture
short chain
Prior art date
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PCT/US2008/014145
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English (en)
Inventor
Alena Kubatova
Wayne Seames
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University of North Dakota UND
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University of North Dakota UND
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Filing date
Publication date
Application filed by University of North Dakota UND filed Critical University of North Dakota UND
Priority to AU2008343713A priority Critical patent/AU2008343713B9/en
Priority to JP2010541443A priority patent/JP2011519344A/ja
Priority to BRPI0821663-0A priority patent/BRPI0821663A2/pt
Priority to CA 2711042 priority patent/CA2711042A1/fr
Priority to MX2010007010A priority patent/MX2010007010A/es
Priority to EP08868965.8A priority patent/EP2231830B1/fr
Priority to ES08868965T priority patent/ES2531169T3/es
Publication of WO2009085324A1 publication Critical patent/WO2009085324A1/fr
Priority to IL20629210A priority patent/IL206292A/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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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
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B13/00—Recovery of fats, fatty oils or fatty acids from waste materials
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/003—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with alcohols
    • 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
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes

Definitions

  • the invention described herein provides a process for the production of commercial grade short chain carboxylic acids and short chain carboxylic esters from triacylglycerides, long chain fatty acids, long chain lipids, or similar chemicals.
  • One embodiment of the present invention is a method for producing a mixture of short chain carboxylic acids from biomass.
  • the method includes adding biomass to a reactor vessel, heating the biomass to crack it, removing undesired and unreacted materials and light ends from the cracked biomass, and removing a mixture containing carboxylic acids having carbon chain lengths between C2 and Cl 6.
  • Another embodiment of the present invention is a composition including a carboxyl group-containing compound derived by cracking biomass and having a carboxyl carbon chain length between C2 and Cl 6.
  • an oil containing primarily fatty acids embedded within triacylglyceride obtained from plants, expressed from algae, derived from animal biomass, or derived from other sources is added to a reactor vessel.
  • the oil is heated in the reactor vessel to a temperature from about 100 0 C to about 600 0 C at a pressure ranging from about vacuum conditions to about 3000 psia for a time sufficient to crack the oil.
  • a pressure ranging from about vacuum conditions to about 3000 psia for a time sufficient to crack the oil.
  • undesired material, unreacted oil, and light ends are removed from the cracked oil.
  • the purified material contains chemical compounds that are desirable for isolation as short chain carboxylic acids and fuels.
  • short chain carboxylic acid compounds are extracted from fuel compounds and are purified.
  • the short chain carboxylic acids generally include fatty acids with 2-12 carbon atoms (C2-C12).
  • Desirable fuel components generally include C4-C16 alkanes, alkenes, aromatics, cycloparaffins, and alcohols.
  • preferential extraction of selected fatty acids is carried out by liquid-liquid extraction using a basic aqueous solvent such as an amine like trimethylamine.
  • a basic aqueous solvent such as an amine like trimethylamine.
  • the fatty acid rich solvent is regenerated to liberate the fatty acids from the solvent.
  • Individual C2-C12 fatty acids are obtained in purified form by physical and/or chemical separation.
  • preferential extraction of selected fatty acids is carried out by a sequential liquid-liquid extraction method whereby room temperature water is used to preferentially extract C2-C5 fatty acids, then higher temperature water or a basic aqueous solution is used to selectively extract C4-C7 fatty acids, and finally pressurized hot water or another solvent is used to preferentially extract C6-C12 fatty acids. After extraction individual C2-C12 fatty acids are obtained in purified form by physical and/or chemical separation. In a sixth aspect of the invention, esterification of one or more of the individual
  • Esterification alcohols employed for the esterification include, but are not limited to, methanol, ethanol, normal propanol, iso-propanol, normal butanol, iso-butanol, allyl alcohol, and other alcohols. After esteriflcation, the esterified material is separated from unreacted material.
  • FIG. 1 is a simplified block diagram illustrating one embodiment of a short chain carboxylic acid production process.
  • FIG. 2 is a simplified block diagram illustrating one embodiment of a short chain carboxylic acid extraction process.
  • FIG. 3 is a simplified block diagram illustrating one embodiment of a short chain carboxylic acid purification process.
  • FIG. 4 is a graph illustrating fatty acid extraction with trimethylamine.
  • FIG. 5 illustrates an ASPEN Plus simulation model for a series of distillation columns to separate and purify short chain carboxylic acids.
  • Biofuel means any fuel that is derived from plant or animal biomass.
  • Biomass means any organic, non-fossil material that is derived from the mass of any biological organism excluding mass that has been transformed by geological processes in substances such as coal or petroleum.
  • Biomass oil means any oil derived from a biomass source.
  • Carboxyl group means a portion of a chemical molecule that contains a carbon atom with a double bond connection to an oxygen atom and where the same carbon atom is also connected to a hydroxyl group, and where no other atoms are connected by a chemical bond to the doubly-bonded oxygen atom.
  • This structure is acidic because in certain solutions, the hydrogen atom on the hydroxyl group readily dissociates from the chemical molecule, forming a cation (the hydrogen atom) and an anion (the remainder of the chemical molecule).
  • Catalyst means those substances that accelerate the rate or ease of a chemical reaction.
  • Catalytic cracking means a cracking process that uses a catalyst.
  • Crossing means any process that changes the chemical composition of an organic chemical or chemical mixture by cleaving one or more carbon-carbon bonds in one or more molecules.
  • Crop means any plant.
  • Diesel means a fuel made commercially for diesel-powered vehicles.
  • Carboxylic acid ester is a chemical compound formed by the reaction of a carboxylic acid and an alcohol, where a terminal hydrogen atom of the carboxyl group is replaced by a carbon chain (radical) from the alcohol.
  • “Fatty acid” means a carboxylic acid with a saturated or unsaturated aliphatic tail.
  • Hydroxyl group means a portion of a chemical molecule containing an oxygen atom connected by a single bond to a hydrogen atom and also connected by a single bond to the rest of the chemical molecule, where the hydrogen atom is not connected to any other atoms.
  • Light ends means chemicals which stay in the gaseous phase at conditions of temperature and pressure at which middle distillates are in the liquid phase.
  • Middle distillate means a chemical which has properties amenable for inclusion in a gasoline, kerosene, or diesel type fuel or which have a volatility similar to those paraffins and/or olefins which are amenable for inclusion in a gasoline, kerosene, or diesel type fuel.
  • a middle distillate can also contain carboxylic acids.
  • Plant means any living organism that is a member of the kingdom Plantae or of the division Chiorphyta (green algae).
  • Plant oil means lipids that are derived from plant sources. Examples of plant oil include crop oils or oilseeds and vegetable oils.
  • Plant oil includes crop oils or oilseeds and vegetable oils.
  • Short chain carboxylic acid means a chemical compound with no more than 12 carbons that contains a carboxyl group.
  • Short chain carboxylic ester means a chemical compound derived from a short chain carboxylic acid in which the carboxylic acid group is replaced by an ester group.
  • Thermal cracking means a cracking process that involves the addition of energy in the form of thermal energy as measured by an increase in the temperature of the substance being cracked.
  • Triacylglyceride or "TG” is a major component of unmodified plant oils, it is an ester of glycerol and three fatty acids.
  • Unreacted raw material is the material in the cracking reactor product stream that has a chemical composition that is not amenable as a middle distillate blend component and can be further exposed to cracking reactor conditions and transformed into middle distillate and/or light ends and/or tars.
  • These compounds may be chemically identical to the original starting material, a fatty acid whose length is identical or similar to the fatty acid chains on an original triacylglyceride (when triacylglycerides are in the feedstock) or a partially cracked paraffin, olefin, or carboxylic acid that has too many carbon atoms in the primary carbon chain to be amenable as a middle distillate blend component.
  • the present invention is directed to the production and purification of C2 to Cl 6 short chain carboxylic acids with potentially subsequent conversion to short chain carboxylic esters from plant oils, biologically generated lipids, or animal fats.
  • the feedstocks are triacylglyceride compounds.
  • This invention provides a means to produce these valuable and necessary chemicals from new feedstocks, not currently utilized in their production.
  • the chemical modifications, based on the use of cracking and separation techniques, are designed to produce commercial-quality short chain carboxylic acid chemical products that can directly replace comparable chemical products generated from other feedstock sources.
  • Route I 3 Route 2 b (safflower oil, high in
  • Olefins C 5 -C 10 12.0
  • Route 1 is catalytic cracking at low temperature: Alencar, 1983; at 300 0 C;
  • Route 2 is catalytic cracking at high temperature: Katikaneni, 1995; at 450 °C;
  • 0 Route 3 is non-catalytic cracking at low temperature: Schwab, 1988; at 300-360
  • the resulting middle distillate contains 5% or more short chain carboxylic acids, preferably 20% or more short chain carboxylic acids, more preferably 30% or more short chain carboxylic acids, and most preferably 60% or more short chain carboxylic acids.
  • the present invention uses thermal or catalytic cracking technologies known in the art coupled with separation technologies such as distillation, filtration, solvent extraction, and related technologies, for the specific purpose of producing commercial quality short chain carboxylic acids from biomass. Previously, these same short chain carboxylic acids were produced from sources other than biomass.
  • the raw material for this new process is any triacylglyceride, free fatty acid or other carboxylic acid representing a group of chemical compounds that can be found in plants or plant oils or medium (C 10-Cl 4) and longer (greater than C 16) chain fatty acids that are naturally synthesized and found in biomass such as algae, animal fats, or modified materials.
  • the triacylglycerides in plant oils generally contain three medium (C10-C14) and/or long (greater than C16) chain fatty (naturally synthesized carboxylic) acids connected via a glycerol group. These medium and/or long chain fatty acids, can be purified, separated, and chemically modified for use as a food source or chemical feedstock or as a potential transportation fuel.
  • Plants and plant oils include, but are not limited to, flax, soybean, safflower, sunflower, sesame, canola, rapeseed, jatropha, primrose, poppy, camelina, crambe, olive, coconut, palm, cotton, corn, soybean, jojoba, pennycress, tomato and nuts. Compositions of some major commercially-available crop oils are listed in Table 3.
  • Typical fatty acids contained in crop oils include saturated and unsaturated fatty acids. Saturated fatty acids do not contain any double bonds or other functional groups. Unsaturated fatty acids contain two or more carbon atoms having a carbon-carbon double bond. Saturated acids include stearic (C18; 18:0), palmitic (C16; 16:0), myristic (C14; 14:0), and lauric (C12; 12:0).
  • Unsaturated acids include those such as linolenic (cis, cis, cis Cl 8; 18:3), linoleic (cis, cis Cl 8; 18:2), oleic (cis Cl 8; 18:1), hexadecanoic (cis, cis C16; 16:2), palmitoleic (cis C16; 16:1), and myristoleic (cis C14; 14:1). It is known that thermal and catalytic cracking of medium (C 10-Cl 4) and/or long
  • the present invention describes a process that can produce short chain carboxylic acids and carboxylic acid esters while also producing materials suitable for use fuels or fuel blendstocks.
  • Combining production of short chain carboxylic acids and acid esters with fuel or fuel products offers the ability to produce not one but two beneficial products using one set of cracking parameters.
  • energy is used to break carbon-carbon bonds. Once broken, each carbon atom ends up with a single electron and free radicals. Reactions of the free radicals can lead to the various products illustrated in Table 1.
  • the breaking of large organic molecules into smaller, and more useful, molecules can be achieved by using high pressures and/or temperatures with a catalyst (catalytic cracking) or without (thermal cracking).
  • FIG. 1 is a simplified block flow diagram of one embodiment of the short chain carboxylic acid production process.
  • Biomass (including crop oils, lipids and animal fat feedstocks) 10 is produced by processes now available or that may be discovered in the future. Biomass 10 may be preheated or directly fed into a cracking reactor for thermal cracking step 12. By varying the time, temperature, and pressure under which a particular feedstock remains under cracking conditions, the desired degree of cracking (conversion) can be controlled. Temperature and time (residence time) are the more important process variables with pressure playing a secondary role. The products of the cracking process are dependent upon the conditions of cracking and the original composition of biomass 10 and the gaseous environment present in the cracking reactor.
  • biomass 10 is heated to a temperature ranging from 100 °C to 600 °C at pressures ranging from vacuum conditions to 3000 psia in the cracking reactor for residence times ranging from one to 180 minutes.
  • the temperature range is more preferably 300 0 C to 500 0 C and most preferably 390 °C to 440 °C.
  • the cracking conditions are varied based on detailed chemical analyses in order to produce the optimal mixture of short chain carboxylic acids and fuel components.
  • a catalyst can be used to improve the yield of desirable products, decrease the formation of unwanted products, or increase the efficiency of the cracking reaction due to lower pressure, temperature, or residence time requirements.
  • Catalysts include but are not limited to zeolites, carbon and rare metals such as palladium, niobium, molybdenum, platinum, titanium, aluminum, cobalt, gold and mixtures thereof.
  • the cracking output is subjected to a variety of processing and purification steps 14 dependent upon the material generated.
  • the output from the cracking reactor depends upon the specific reactor design employed. The following are examples of reactor types known to those skilled in the art: batch, continuous flow through, flow through packed bed, and fluidized bed.
  • Material generated in the cracking reactor can generally be defined as light ends 16, unreacted raw materials (recyclables) 18, residual materials or residue (tars) 20, and middle distillate 22.
  • Light ends 16 are unreacted vapor-phase materials that were added to the reactor to manipulate the cracking reaction, such as hydrogen, nitrogen, or water vapor, in addition to small molecular weight organic chemicals and hydrocarbons generated in the cracking reactor.
  • the small molecular weight organic chemicals and hydrocarbons such as methane, methanol, ethane, ethanol, «-pentane, z-pentane, pentene, pentanol n-butane, z-butane, butanol, butane, methyl ester, ethyl ester, etc., have chemical and physical properties that are undesirable (such as being too volatile) when present in substantial concentrations of short chain carboxylic acid extracts or middle distillate fuel components.
  • Light ends are separated from the other material that exits the reactor by gas-liquid phase separation, distillation, condensation, or other processes in purification step 14.
  • Unreacted raw materials 18 are chemicals that enter the cracking reactor but are not converted to chemical compounds with carbon chains shorter than Cl 6. These materials have some chemical and physical properties that are undesirable in the fuel products. Unreacted raw materials are separated from the middle distillate components by distillation or other separation techniques in purification step 14. Unreacted or uncracked raw materials 18 can then be returned to the cracking reactor, fed to a second cracking reactor or utilized for some other purpose.
  • Residual material or residue tars 20 are chemicals produced during cracking reactions that have a higher molecular weight, lower volatility and/or lower heating value than is desirable in middle distillate 22. Some of the residual components 20 can be separated from middle distillate 22 along with unreacted raw materials 18 and processed with these unreacted raw materials 18. Other residue components 20, typically those of higher molecular weight, will be in the form of solid material (at room temperature) after the cracking reaction. These compounds are typically known as "tars.” Tars 20 may contain valuable chemical compounds, such as boiler fuel or other by-products that can be extracted from residual material 20 by various process methods including solvent extraction, distillation, etc or may contain chemicals that can be transformed by chemical reactions into valuable chemical compounds. Depending upon the design of the cracking reactor, tars 20 may not be amenable to further processing. Such tars 20 may be oxidized, combusted or otherwise removed from the cracking reactor or cracking catalysts by methods known in the art.
  • Middle distillate components 22 are short chain carboxylic acid compounds generated in the cracking reactor as well as those portions of the remaining material that contribute to desirable chemical and physical properties of fuel or fuel blend stock products.
  • Short chain carboxylic acids 28 are removed from middle distillate 22 using one or more process methods (step 24) including solvent extraction, distillation, etc.
  • Middle distillate 22 enters a short chain fatty acid (SCFA) extraction column in step 30.
  • Solvent such as a 40% aqueous solution of trimethylamine, hot water or aqueous NaOH, is delivered to the extraction column.
  • the solvent absorbs short chain fatty acids as it passes through the column, generating an SCFA-rich solvent while other components (e.g., biofuel components 26) remain in a separate liquid phase and are removed from the column separately.
  • Mixed short chain fatty acids 28 are separated from the solvent.
  • the solvent can then be regenerated (step 32) and delivered back to the extraction column.
  • short chain carboxylic (fatty) acids 28 are isolated from middle distillate 22, they can be processed and purified further. Additional purification steps produce product streams that contain primarily single components or specific groups of short chain carboxylic acids 28.
  • One embodiment of a typical purification scheme is shown in FIG. 3. Light fatty acids (C5 and shorter) and heavy fatty acids (C6 to C 16) are separated from mixed short chain fatty acids 28 by mixed SCFA splitter 34. The separated fatty acids are then further separated using distillation columns to extract fatty acids of particular carbon chain lengths. For example, the light short chain fatty acids are delivered to a series of distillation columns.
  • Acetic acid is isolated in acetic acid column 36, propanoic acid is isolated in propanoic acid column 38, butyric acid is isolated in butyric acid column 40 and valeric acid is isolated in valeric acid column 42.
  • Less volatile (heavy) short chain fatty acids are isolated in a similar manner using hexanoic acid column 44, heptanoic acid column 46 and heavy SCFA splitter 48 (for fatty acids having eight or more carbon atoms on the carbon chain).
  • the purification process selected is dependent upon the technology used to isolate short chain carboxylic acids 28 from the fuel components of middle distillate 22.
  • short chain carboxylic acids 28 produced in this process can be further processed into short chain carboxylic acid esters by reacting the short chain carboxylic acid with one or more alcohols. Unreacted and/or by-product material is then removed from the product short chain carboxylic acid esters to obtain commercial quality short chain carboxylic acid esters.
  • a triacylglyceride crop oil, biologically generated lipid, animal fat oil or a transesterified derivative of any of these oils is heated to a temperature ranging from 300 °C to 500 °C, in a cracking reactor, at pressures ranging from vacuum conditions to 3000 psia, in the presence of a gaseous environment that can contain an inert gas such as nitrogen, water vapor, hydrogen, a mixture of vapor-phase organic chemicals or any other gaseous substance, for residence times ranging from one to 180 minutes to affect cracking reactions that change the chemical composition of the contents of the cracking reactor.
  • an inert gas such as nitrogen, water vapor, hydrogen, a mixture of vapor-phase organic chemicals or any other gaseous substance
  • the vapor leaving the cracking reactor (crackate), is subjected to downstream processing that can include cooling and partial condensation, vapor/liquid separation, extraction of by-product chemicals by solvent extraction or other chemical/physical property manipulation, in-situ reaction, distillation or flash separation to produce an acceptable transportation fuel, such as aviation turbine fuel or diesel fuel.
  • the liquid and solids leaving the reactor are subjected to downstream processing that can include cooling or heating, liquid/solid separation, vapor/liquid separation, vapor/solid separation, extraction of by-product chemicals by solvent extraction or other chemical/physical property manipulation to produce an acceptable fuel by-product or byproducts.
  • Unreacted and partially reacted material 22 separated from either the crackate or the residue may be recycled to the cracking reactor, routed to additional cracking reactors or used in other processes.
  • Example 1 Short Chain Fatty Acid Production from Soybean Oil
  • a two liter per hour continuous cracking reactor system was used as the cracking reactor. Thermal cracking under vacuum conditions was applied to soybean oil. Output from the cracking reactor (crackate) was analyzed and then processed further. The light hydrocarbons were removed in a packed distillation column, and the heaviest were removed using a second packed distillation column. This produced a middle distillate liquid containing a high percentage of short chain carboxylic acids. The middle distillate was then mixed with an equal amount of room temperature, purified water and the oil and water phases were then separated.
  • a middle distillate 18 containing a high percentage of short chain carboxylic acids was produced from soybean oil.
  • Middle distillate 18 was then mixed in a separatory funnel with a 25% (w/w) aqueous solution of trimethylamine at room temperature.
  • the amount of aqueous amine solution added was such that 0.002 moles of trimethylamine were present for each gram of middle distillate 18.
  • the aqueous and organic phases were then separated and the acid number of middle distillate 18 was measured according to ASTM method D3242.
  • FIG. 4 illustrates the results of the short chain fatty acid extraction with aqueous amine.
  • Distillation column T300 separates the two carbon fatty acid (acetic acid) from the three carbon fatty acid (propanoic acid). Likewise, fatty acids having four or five carbon atoms are sent from distillation column T200 to distillation column T500. Distillation column T500 separates the four carbon fatty acid (butyric acid) from the five carbon fatty acid (valeric acid). In a similar fashion, distillation column T800 separates fatty acids having six or seven carbon atoms from those having eight or more. Fatty acids having six or seven carbon atoms are sent to distillation column T900 where the six carbon fatty acid (hexanoic acid) is separated from the seven carbon fatty acid (heptanoic acid). Estimated yields are listed in FIG. 5 for the simulated purification.
  • the method of producing short chain carboxylic acids and acid esters described herein provides a useful tool for creating valuable chemical compounds from biomass rather than petroleum precursors.
  • the method also allows for the coproduction of chemical compounds useful in fuel applications using the same cracking parameters. Efficiency gains are realized by being able to generate two sets of useful chemical compounds using steps that share some of the same processing conditions.

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  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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Abstract

L'invention porte sur un procédé de production d'un mélange d'acides carboxyliques à chaîne courte (28) à partir de la biomasse (10). Ce procédé comprend l'addition de biomasse (10) dans un récipient de réacteur, le chauffage de la biomasse pour la craquer, l'élimination de matières indésirées (20) et n'ayant pas réagi (18) et de fractions légères (16) à partir de la biomasse craquée, et l'élimination d'un mélange contenant des acides carboxyliques ayant des longueurs de chaîne carbonée entre C2 et C16 (24). Une composition comprend un composé à teneur en groupe carboxyle (28) issu d'un craquage de biomasse (10) et ayant une longueur de chaîne carbonée carboxylée entre C2 et C16.
PCT/US2008/014145 2007-12-31 2008-12-31 Procédé de production d'acides et esters carboxyliques à chaîne courte à partir de la biomasse et produit obtenu par ce procédé Ceased WO2009085324A1 (fr)

Priority Applications (8)

Application Number Priority Date Filing Date Title
AU2008343713A AU2008343713B9 (en) 2007-12-31 2008-12-31 Method for production of short chain carboxylic acids and esters from biomass and product of same
JP2010541443A JP2011519344A (ja) 2007-12-31 2008-12-31 バイオマスから短鎖カルボン酸とエステルを生産する方法並びにその生成物
BRPI0821663-0A BRPI0821663A2 (pt) 2007-12-31 2008-12-31 Método para a produção de ésteres e ácidos carboxílicos de cadeia curta a partir de biomassa e produto da mesma
CA 2711042 CA2711042A1 (fr) 2007-12-31 2008-12-31 Procede de production d'acides et esters carboxyliques a chaine courte a partir de la biomasse et produit obtenu par ce procede
MX2010007010A MX2010007010A (es) 2007-12-31 2008-12-31 Metodo de produccion de acidos carboxilicos y esteres de cadena corta a partir de biomasa y producto del mismo.
EP08868965.8A EP2231830B1 (fr) 2007-12-31 2008-12-31 Procédé de production d'acides et esters carboxyliques à chaîne courte à partir de la biomasse et produit obtenu par ce procédé
ES08868965T ES2531169T3 (es) 2007-12-31 2008-12-31 Procedimiento de producción de ácidos y ésteres carboxílicos de cadena corta de biomasa y producto del mismo
IL20629210A IL206292A (en) 2007-12-31 2010-06-10 A method for producing a short chain of carboxylic acids and esters from biomass @ and product @ the method

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US7420607P 2007-12-31 2007-12-31
US61/074,206 2007-12-31

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JP (1) JP2011519344A (fr)
AU (1) AU2008343713B9 (fr)
BR (1) BRPI0821663A2 (fr)
CA (1) CA2711042A1 (fr)
IL (1) IL206292A (fr)
MX (1) MX2010007010A (fr)
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US8906236B2 (en) 2010-07-26 2014-12-09 Sapphire Energy, Inc. Process for the recovery of oleaginous compounds and nutrients from biomass
US9028696B2 (en) 2010-07-26 2015-05-12 Sapphire Energy, Inc. Process for the recovery of oleaginous compounds from biomass
WO2018109644A1 (fr) * 2016-12-12 2018-06-21 Sabic Global Technologies B.V. Procédé de distillation d'acides gras provenant d'huile de palmiste pour un minimum de déchets

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US20070014895A1 (en) * 2005-07-12 2007-01-18 Holtzapple Mark T System and Method for Converting Biomass
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Publication number Priority date Publication date Assignee Title
US8192628B2 (en) 2010-07-26 2012-06-05 Sapphire Energy, Inc. Process for the recovery of oleaginous compounds from biomass
US8882861B2 (en) 2010-07-26 2014-11-11 Sapphire Energy, Inc. Oleaginous compounds from biomass
US8906236B2 (en) 2010-07-26 2014-12-09 Sapphire Energy, Inc. Process for the recovery of oleaginous compounds and nutrients from biomass
US9028696B2 (en) 2010-07-26 2015-05-12 Sapphire Energy, Inc. Process for the recovery of oleaginous compounds from biomass
WO2018109644A1 (fr) * 2016-12-12 2018-06-21 Sabic Global Technologies B.V. Procédé de distillation d'acides gras provenant d'huile de palmiste pour un minimum de déchets
CN110268041A (zh) * 2016-12-12 2019-09-20 乔治洛德方法研究和开发液化空气有限公司 从棕榈仁油中蒸馏脂肪酸以使废物最少化的方法
US10577559B2 (en) 2016-12-12 2020-03-03 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Process for distillation of fatty acids from palm kern oil for minimum waste

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CA2711042A1 (fr) 2009-07-09
AU2008343713B2 (en) 2013-08-01
BRPI0821663A2 (pt) 2015-06-16
JP2011519344A (ja) 2011-07-07
AU2008343713B9 (en) 2014-02-27
MX2010007010A (es) 2010-12-20
IL206292A (en) 2013-07-31
AU2008343713A1 (en) 2009-07-09

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