JP2011026567A5 - - Google Patents

Download PDF

Info

Publication number
JP2011026567A5
JP2011026567A5 JP2010142474A JP2010142474A JP2011026567A5 JP 2011026567 A5 JP2011026567 A5 JP 2011026567A5 JP 2010142474 A JP2010142474 A JP 2010142474A JP 2010142474 A JP2010142474 A JP 2010142474A JP 2011026567 A5 JP2011026567 A5 JP 2011026567A5
Authority
JP
Japan
Prior art keywords
reaction mixture
fatty acid
steryl glucoside
glycerin
alkyl ester
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.)
Granted
Application number
JP2010142474A
Other languages
Japanese (ja)
Other versions
JP5618648B2 (en
JP2011026567A (en
Filing date
Publication date
Application filed filed Critical
Priority to JP2010142474A priority Critical patent/JP5618648B2/en
Priority claimed from JP2010142474A external-priority patent/JP5618648B2/en
Publication of JP2011026567A publication Critical patent/JP2011026567A/en
Publication of JP2011026567A5 publication Critical patent/JP2011026567A5/ja
Application granted granted Critical
Publication of JP5618648B2 publication Critical patent/JP5618648B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Claims (9)

ステリルグルコシドを溶解した状態で含有する油脂と低級アルコールとをエステル交換反応させて反応混合物を得る工程と、その後、該反応混合物中にステリルグルコシド析出させる工程と、
該反応混合物からステリルグルコシドを分離する工程とを有する、脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法であって、
該エステル交換反応が、油脂由来の脂肪酸の脂肪酸低級アルキルエステルへの変換率が90%以上となるまで行う工程である、脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法
A step of transesterifying the fat and oil containing the steryl glucoside in a dissolved state with a lower alcohol to obtain a reaction mixture, and then a step of precipitating steryl glucoside in the reaction mixture ;
Separating the steryl glucoside from the reaction mixture, the method for producing fatty acid lower alkyl ester, glycerin and steryl glucoside ,
A method for producing a fatty acid lower alkyl ester, glycerin and steryl glucoside, wherein the transesterification reaction is performed until the conversion rate of fatty acid derived from fats and oils to a fatty acid lower alkyl ester reaches 90% or more .
工程(a):ステリルグルコシドを溶解した状態で含有する油脂と低級アルコールとをエステル交換反応させる工程、Step (a): A step of transesterifying the fat and oil containing steryl glucoside in a dissolved state with a lower alcohol,
工程(b):工程(a)より得られた反応混合物を油水分離する工程、Step (b): a step of oil-water separation of the reaction mixture obtained from the step (a),
工程(c):工程(b)で得られた油相と低級アルコールとをエステル交換反応させる工程、Step (c): a step of transesterifying the oil phase obtained in step (b) with a lower alcohol,
工程(d):工程(c)より得られた反応混合物中にステリルグルコシドを析出させる工程、Step (d): a step of precipitating steryl glucoside in the reaction mixture obtained from step (c),
工程(e):工程(d)より得られた反応混合物からステリルグルコシドを分離する工程、Step (e): a step of separating steryl glucoside from the reaction mixture obtained from step (d),
工程(f):工程(e)により分離された反応混合物を油水分離し、脂肪酸アルキルエステル及びグリセリンを得る工程を含む、請求項1記載の脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法。Step (f): The method for producing a fatty acid lower alkyl ester, glycerol and steryl glucoside according to claim 1, comprising a step of oil-water separation of the reaction mixture separated in step (e) to obtain a fatty acid alkyl ester and glycerol.
前記エステル交換反応工程で得られる反応混合物が、脂肪酸低級アルキルエステル、未反応油脂、グリセリン、低級アルコール、及びステリルグルコシドを含む混合物で、2相に分離した状態のものを得る工程であり、The reaction mixture obtained in the transesterification reaction step is a step of obtaining a mixture separated into two phases in a mixture containing a fatty acid lower alkyl ester, unreacted oil, glycerin, lower alcohol, and steryl glucoside,
前記応混合物中にステリルグルコシドを析出させる工程が、前記2相の中間にステリルグルコシドの白色析出物を析出させる工程である、請求項1又は2記載の脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法。The fatty acid lower alkyl ester, glycerin and steryl according to claim 1 or 2, wherein the step of precipitating steryl glucoside in the reaction mixture is a step of precipitating a white precipitate of steryl glucoside in the middle of the two phases. Production method of glucoside.
前記2相が脂肪酸メチルエステルを含む相及びグリセリンを含む相である、請求項3記載の脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法。The method for producing a fatty acid lower alkyl ester, glycerin and steryl glucoside according to claim 3, wherein the two phases are a phase containing a fatty acid methyl ester and a phase containing glycerin. 前記反応混合物中にステリルグルコシドを析出させる工程が、反応混合物の温度を低下させる工程である、請求項1〜4の何れか1項記載の脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法。The method for producing fatty acid lower alkyl ester, glycerin and steryl glucoside according to any one of claims 1 to 4, wherein the step of precipitating steryl glucoside in the reaction mixture is a step of lowering the temperature of the reaction mixture. . 前記反応混合物中にステリルグルコシドを析出させる工程が、反応混合物の温度を30〜35℃に調整する工程である、請求項1〜4の何れか1項記載の脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法。The step of precipitating steryl glucoside in the reaction mixture is a step of adjusting the temperature of the reaction mixture to 30 to 35 ° C, wherein the fatty acid lower alkyl ester, glycerin and stearic acid according to any one of claims 1 to 4. A method for producing rilglucoside. 前記反応混合物からステリルグルコシドを分離する工程が、反応混合物をろ過して分離する工程である、請求項1〜6の何れか1項記載の脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法。 The method for producing a fatty acid lower alkyl ester, glycerin and steryl glucoside according to any one of claims 1 to 6, wherein the step of separating steryl glucoside from the reaction mixture is a step of filtering and separating the reaction mixture. . 前記エステル交換反応工程で得た反応混合物から、反応混合物中の低級アルコール濃度を8質量%以下になるまで低級アルコールを除去する工程を含む、請求項1〜の何れか1項記載の脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法。 The fatty acid lower of any one of claims 1 to 7 , comprising a step of removing the lower alcohol from the reaction mixture obtained in the transesterification reaction step until the lower alcohol concentration in the reaction mixture becomes 8% by mass or less. A process for producing alkyl esters, glycerin and steryl glucoside. エステル交換反応工程が、固体酸触媒を用いて行う工程である、請求項1〜の何れか1項記載の脂肪酸低級アルキルエステル、グリセリン及びステリルグルコシドの製造法。 The method for producing a fatty acid lower alkyl ester, glycerin and steryl glucoside according to any one of claims 1 to 8 , wherein the transesterification reaction step is a step performed using a solid acid catalyst.
JP2010142474A 2009-06-30 2010-06-23 Process for producing fatty acid lower alkyl ester, glycerin and steryl glucoside Active JP5618648B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2010142474A JP5618648B2 (en) 2009-06-30 2010-06-23 Process for producing fatty acid lower alkyl ester, glycerin and steryl glucoside

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2009155423 2009-06-30
JP2009155423 2009-06-30
JP2010142474A JP5618648B2 (en) 2009-06-30 2010-06-23 Process for producing fatty acid lower alkyl ester, glycerin and steryl glucoside

Publications (3)

Publication Number Publication Date
JP2011026567A JP2011026567A (en) 2011-02-10
JP2011026567A5 true JP2011026567A5 (en) 2011-11-24
JP5618648B2 JP5618648B2 (en) 2014-11-05

Family

ID=43411158

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2010142474A Active JP5618648B2 (en) 2009-06-30 2010-06-23 Process for producing fatty acid lower alkyl ester, glycerin and steryl glucoside

Country Status (5)

Country Link
JP (1) JP5618648B2 (en)
CN (1) CN102459307B (en)
BR (1) BRPI1015067B1 (en)
MY (1) MY162664A (en)
WO (1) WO2011002090A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE535398C2 (en) * 2011-01-21 2012-07-24 Perstorp Ab Process for the purification of biodiesel with self-cleaning filters
EP2812063B1 (en) 2012-02-08 2020-03-25 Avenu Medical, Inc. Intravascular arterial to venous anastomosis and tissue welding catheter
CN116103167A (en) * 2023-02-09 2023-05-12 南京工业大学 Wilkham yeast with abnormal characteristics, and separation method and application thereof

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07310090A (en) * 1994-05-19 1995-11-28 Tensei Seiyu Kk Production of fatty acid methyl ester
FR2752242B1 (en) * 1996-08-08 1998-10-16 Inst Francais Du Petrole PROCESS FOR THE MANUFACTURE OF ESTERS FROM VEGETABLE OR ANIMAL OILS AND ALCOHOLS
JP3594553B2 (en) * 2000-12-05 2004-12-02 昭和産業株式会社 How to fractionate soy glycolipids
JP5154015B2 (en) * 2005-12-20 2013-02-27 花王株式会社 Process for producing fatty acid alkyl ester and glycerin
US20070151146A1 (en) * 2005-12-29 2007-07-05 Inmok Lee Processes of Producing Biodiesel and Biodiesel Produced Therefrom
US9109170B2 (en) * 2006-02-02 2015-08-18 Reg Biofuels, Llc Biodiesel cold filtration process
US8039651B2 (en) * 2007-10-31 2011-10-18 Nippon Shokubai Co., Ltd. Method for producing fatty acid alkyl ester and/or glycerin
EP2197995A4 (en) * 2007-11-22 2011-06-15 Nippon Catalytic Chem Ind Method for producing fatty acid alkyl esters and/or glycerin using fat or oil
JP2009155476A (en) * 2007-12-26 2009-07-16 Nippon Shokubai Co Ltd Method and apparatus for producing fatty acid alkyl ester and/or glycerin

Similar Documents

Publication Publication Date Title
Vo et al. Kinetics study of the hydrothermal liquefaction of the microalga Aurantiochytrium sp. KRS101
Tran et al. An effective acid catalyst for biodiesel production from impure raw feedstocks
WO2011012440A3 (en) A process for the production of bio-naphtha from complex mixtures of natural occurring fats & oils
MY145667A (en) Process for producing fatty acid alkyl esters and glycerin
RU2012149617A (en) LIQUID OIL AND METHOD FOR PRODUCING IT
CN102965404B (en) Preparation method of high-purity diglyceride
WO2007059512A3 (en) Transesterification of oil to form biodiesels
ITMI20071368A1 (en) NEW PROCESS FOR THE PRODUCTION OF ESTERS FROM VEGETABLE OILS AND / OR ANIMAL FATS WITH THE USE OF HETEROGENEOUS CATALYSTS, IN PARTICULAR IN THE PRESENCE OF FREE ACIDITY AND WATER.
WO2014111598A3 (en) Process for the production of bio-naphtha from complex mixtures of natural occurring fats & oils
MY156764A (en) Method for producing fats and oils
JP2010515799A5 (en)
MY156807A (en) Method for producing regenerated clay, regenerated clay, and method for producing purified fats and oils
JP2010516627A (en) Method for separating saturated and unsaturated fatty acids
ES2728062T3 (en) Preparation procedure of fatty acid alkyl ester using fat
JP2015527060A5 (en)
JP2011026567A5 (en)
MY179408A (en) Production of products from feedstocks containing free fatty acids
WO2010141917A3 (en) Process for continuous production of biodiesel from fatty acid containing feedstocks
MY169494A (en) Process for producing fatty acid esters
JP2010013511A (en) Biodiesel fuel and method for producing the same
MY162664A (en) Method for producing fatty acid lower alkyl ester, glycerol, and steryl glucoside
RO128691A8 (en) Process for preparing a fuel for diesel engines
KR20110094013A (en) Method for the transesterification of hydroxylated oils
MY176376A (en) Recovery of tocopherols/tocotrienols, glycerine, sterols and fatty acid esters from vegetable oil distillate and the process thereof
Montero et al. Fatty acids recovery from microalgae for biodiesel production