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WO2008011731A3 - A device for the transesterification of animal and plant glycerides into fatty acid alkyl esters for small scale production of biodiesel and value added products - Google Patents

A device for the transesterification of animal and plant glycerides into fatty acid alkyl esters for small scale production of biodiesel and value added products Download PDF

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Publication number
WO2008011731A3
WO2008011731A3 PCT/CA2007/001875 CA2007001875W WO2008011731A3 WO 2008011731 A3 WO2008011731 A3 WO 2008011731A3 CA 2007001875 W CA2007001875 W CA 2007001875W WO 2008011731 A3 WO2008011731 A3 WO 2008011731A3
Authority
WO
WIPO (PCT)
Prior art keywords
primary vessel
glycerides
fatty acid
alkyl esters
small scale
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/CA2007/001875
Other languages
French (fr)
Other versions
WO2008011731A2 (en
WO2008011731B1 (en
Inventor
Norman R Jaehrling
John Barbeau
Luc C Duchesne
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.)
FOREST BIOPRODUCTS Inc
Original Assignee
FOREST BIOPRODUCTS Inc
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 FOREST BIOPRODUCTS Inc filed Critical FOREST BIOPRODUCTS Inc
Publication of WO2008011731A2 publication Critical patent/WO2008011731A2/en
Publication of WO2008011731A3 publication Critical patent/WO2008011731A3/en
Publication of WO2008011731B1 publication Critical patent/WO2008011731B1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/026Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40Characteristics of the process deviating from typical ways of processing
    • C10G2300/4068Moveable devices or units, e.g. on trucks, barges
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00Technologies relating to oil refining and petrochemical industry
    • Y02P30/20Technologies relating to oil refining and petrochemical industry using bio-feedstock

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)
  • Fats And Perfumes (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

The present invention relates to a device for the small scale and portable production of transesterified fatty acid alkyl esters for use as biodiesel or other applications. The invention allows for the economic production in small scale and portable equipment which transesterifies various glycerides including waste vegetable oil, animal fats, and/or virgin vegetable oil singly or in admixtures of various ratios. A primary vessel (1 ) which is fitted with immersion heaters or other heating means (5) contains glycerides which are heated to reaction temperature. A reservoir (2) which contains an alkaline solution, for example sodium or potassium hydroxide dissolved in an alcohol, particularly methanol, is connected to primary vessel (1) with a piping system and in-line pump (4) in a pipe loop which permits the mixture of the glycerides with the strong base and alcohol mixture. Transparent piping, for example transparent tubing (14), is installed on the side of the primary vessel (1) to permit visual examination and act as a manometer. Once transesterification takes place, the bottom phase, which contains glycerol and other residues, is removed through transparent tubing fitted to a clean out pipe mounted at the bottom of the primary vessel (1 ). The resulting fatty acid alkyl esters are then purified by the addition of cleaning reagents, including magnesium silicate in one embodiment or a mild acid in another embodiment, in primary vessel (1).
PCT/CA2007/001875 2006-07-27 2007-07-04 A device for the transesterification of animal and plant glycerides into fatty acid alkyl esters for small scale production of biodiesel and value added products Ceased WO2008011731A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CA002553872A CA2553872A1 (en) 2006-07-27 2006-07-27 A device for the transesterification of animal and plant glycerides intofatty acid alkyd esters for small scale production of biodiesel and value added products
CA2,553,872 2006-07-27

Publications (3)

Publication Number Publication Date
WO2008011731A2 WO2008011731A2 (en) 2008-01-31
WO2008011731A3 true WO2008011731A3 (en) 2008-05-08
WO2008011731B1 WO2008011731B1 (en) 2008-06-26

Family

ID=38981813

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CA2007/001875 Ceased WO2008011731A2 (en) 2006-07-27 2007-07-04 A device for the transesterification of animal and plant glycerides into fatty acid alkyl esters for small scale production of biodiesel and value added products

Country Status (2)

Country Link
CA (1) CA2553872A1 (en)
WO (1) WO2008011731A2 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
UY29851A1 (en) * 2006-10-10 2008-05-02 Barcelo Pedro A Server PROCESS FOR OBTAINING LIQUID HYDROCARBONS FROM THE BREAK OF CARBON MOLECULES AND HYDROGEN
US8097049B2 (en) 2008-02-07 2012-01-17 The Dallas Group Of America, Inc. Biodiesel purification by a continuous regenerable adsorbent process
GR1006523B (en) * 2008-10-23 2009-09-03 Νικολαος Νταϊλιανης Autonomous, portable biofuel production init from unrefined fat of great acidity, as it is produced from units of thermal inactivation of animal byproducts of slaughterhouses with simultaneous removalof fat from the tissues.
US8563482B2 (en) 2010-09-22 2013-10-22 Saudi Arabian Oil Company Environment friendly base fluid to replace the toxic mineral oil-based base fluids
CN102536779B (en) * 2011-06-30 2014-11-26 中国海洋石油总公司 Processing method for preventing seal leakage of circulating pump and purification method of biodiesel
JP2014520918A (en) * 2011-07-15 2014-08-25 ビオミナス・エンゲンハリア・エ・インダストリア・デ・エネルジア・リミターダ Biodiesel education and training equipment and industrial simulation
US9834718B2 (en) 2014-05-06 2017-12-05 Saudi Arabian Oil Company Ecofriendly lubricating additives for water-based wellbore drilling fluids
US11352545B2 (en) 2020-08-12 2022-06-07 Saudi Arabian Oil Company Lost circulation material for reservoir section

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005037969A2 (en) * 2003-10-09 2005-04-28 The Dallas Group Of America, Inc. Purification of biodiesel with adsorbent materials
WO2005052103A1 (en) * 2003-11-24 2005-06-09 Council Of Scientific And Industrial Research An improved process for the preparation of bio-diesel

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005037969A2 (en) * 2003-10-09 2005-04-28 The Dallas Group Of America, Inc. Purification of biodiesel with adsorbent materials
WO2005052103A1 (en) * 2003-11-24 2005-06-09 Council Of Scientific And Industrial Research An improved process for the preparation of bio-diesel

Also Published As

Publication number Publication date
WO2008011731A2 (en) 2008-01-31
CA2553872A1 (en) 2008-01-27
WO2008011731B1 (en) 2008-06-26

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