[go: up one dir, main page]

CN1177024C - Method for producing edible rapeseed protein and oil by aqueous method - Google Patents

Method for producing edible rapeseed protein and oil by aqueous method

Info

Publication number
CN1177024C
CN1177024C CNB021038074A CN02103807A CN1177024C CN 1177024 C CN1177024 C CN 1177024C CN B021038074 A CNB021038074 A CN B021038074A CN 02103807 A CN02103807 A CN 02103807A CN 1177024 C CN1177024 C CN 1177024C
Authority
CN
China
Prior art keywords
protein
oil
precipitate
separate
separator
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.)
Expired - Fee Related
Application number
CNB021038074A
Other languages
Chinese (zh)
Other versions
CN1374383A (en
Inventor
吴文标
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.)
Southwest University
Original Assignee
SOUTHWEST AGRICULTURAL UNIVERSITY
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 SOUTHWEST AGRICULTURAL UNIVERSITY filed Critical SOUTHWEST AGRICULTURAL UNIVERSITY
Priority to CNB021038074A priority Critical patent/CN1177024C/en
Publication of CN1374383A publication Critical patent/CN1374383A/en
Application granted granted Critical
Publication of CN1177024C publication Critical patent/CN1177024C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Peptides Or Proteins (AREA)

Abstract

The present invention relates to a method for producing edible rapeseed protein and oil by an aqueous method. The water solution of sodium sulfite is mixed with rapeseeds; the mixture is processed by jordaning with a pulp residue separator to remove coarse fiber; the pH value of pulp is regulated, and oil and partial protein are precipitated; the oil of the deposition is released by dehydration; the protein is separated with oil by adding hot water; the protein of the concentrated solution is centrifuged or filtrated. The present invention has the advantages of low cost and high extraction rate of protein and oil, and simultaneously, the adverse nutrition factors are removed; the obtained protein and oil can both reach the edible product standard.

Description

水剂法生产食用菜籽蛋白和油脂的方法Method for producing edible rapeseed protein and oil by aqueous method

技术领域technical field

本发明涉及农副产品加工领域,特别是涉及一种水剂法生产食用菜籽蛋白和油脂的方法。The invention relates to the field of agricultural and sideline product processing, in particular to a method for producing edible rapeseed protein and oil by water preparation.

背景技术Background technique

油菜籽中含有相对不利营养的因子,包括1.2-2.5%的植酸,3-7%的硫甙(低硫甙品种为3.5‰左右),0.8-1.6%的酚类化合物,约2.5%棉籽糖和水苏糖,如果不将它们除去,即使作饲料也会阻碍动物的生长发育,不过如在安全范围内食用则有一定的保健作用,因此,通过加工将其进行有效的分离是十分必要的。Rapeseed contains relatively unfavorable nutritional factors, including 1.2-2.5% phytic acid, 3-7% glucosinolates (low glucosinolate varieties are about 3.5‰), 0.8-1.6% phenolic compounds, about 2.5% cottonseed Sugar and stachyose, if they are not removed, will hinder the growth and development of animals even if they are used as feed, but if eaten within a safe range, they will have a certain health effect, so it is very necessary to effectively separate them through processing of.

目前的菜籽加工方法有以下几种:第一种是经过加热蒸炒后榨油,采用这种方法由于引起蛋白质变性及颜色变黑,而导致枯饼的再利用价值降低;第二种是经过机械预榨后,用溶剂浸出油脂,采用这种方法加工的最初设备投资大,使用易燃易爆的溶剂,存在火灾和爆炸的危险,而导致管理成本很高;第三种方法是经过机械预榨后,得到含油量约为10%的枯饼,再用水溶液提取枯饼中的蛋白和油,此乃本发明人前期完成的一项“九五”攻关项目;第四种方法是将菜籽先用机械破碎后,用酸提蛋白质,再用水溶液提油,此乃本发明人已获的一项个人发明专利。The current rapeseed processing methods are as follows: the first one is to extract the oil after heating, steaming and frying. This method will cause protein denaturation and blackening of the color, which will reduce the reuse value of the dry cake; the second is After mechanical pre-pressing, the oil is extracted with a solvent. The initial equipment investment of this method is large, and the use of flammable and explosive solvents has the risk of fire and explosion, which leads to high management costs; the third method is through After mechanical pre-pressing, the dry cake with an oil content of about 10% is obtained, and then the protein and oil in the dry cake are extracted with an aqueous solution. This is a "Ninth Five-Year Plan" research project completed by the inventor in the early stage; the fourth method is After the rapeseed is crushed mechanically, the protein is extracted with acid, and then the oil is extracted with an aqueous solution. This is a personal invention patent obtained by the inventor.

发明内容Contents of the invention

本发明的目的在于提供一种水剂法从未经处理过的原料菜籽中直接用水同时提取食用菜籽蛋白和油脂的方法。该方法用水剂法生产,采用的生产设备和操作程序更简单,既适合于大规模的工业化生产,也适合于小规模的家庭工厂,在同等产量的情况下比榨油法的投入还小,产品质量更高,因此成本低、蛋白质和油提取率高,同时能去掉其中的不利营养因子。The object of the present invention is to provide a method for extracting edible rapeseed protein and oil simultaneously directly from untreated raw rapeseed by water preparation. This method is produced by the water preparation method, and the production equipment and operation procedures adopted are simpler, and it is suitable for both large-scale industrial production and small-scale family factories. The product is of higher quality, so the cost is low and the protein and oil extraction rate is high, and the unfavorable nutritional factors can be removed at the same time.

该方法依次通过下列步骤实现:The method is implemented through the following steps in turn:

1、将油菜籽放入其重量2-15倍的5/1000000-1/1000亚硫酸钠水溶液中,用一装有50-200目筛网的浆渣分离机磨浆除去粗纤维,重复上述步骤2-3次;1. Put the rapeseed into the 5/1000000-1/1000 sodium sulfite aqueous solution which is 2-15 times its weight, and use a pulp separator equipped with a 50-200 mesh screen to refine the pulp to remove the crude fiber, and repeat the above step 2 -3 times;

2、采用离心或精细过滤除尽浆中的残渣,然后将所得的浆调节pH至2-11,用离心机、过滤器或悬液分离器分离含油脂为主的沉淀部分和含有蛋白及其它水溶性物质的上清液;2. Use centrifugation or fine filtration to remove all residues in the slurry, then adjust the pH of the obtained slurry to 2-11, and use a centrifuge, filter or suspension separator to separate the precipitated part mainly containing oil and protein and other supernatant of water-soluble substances;

3、将沉淀用真空或常规的脱水办法脱水,使其含水量达到10-50%破乳,加入沉淀重量1-10倍的60-100℃热水,采用悬液分离器将蛋白溶液和油分开,或采用带加热装置的锥型静止分离器加热1-5小时将蛋白溶液和油分开;3. Dehydrate the precipitate with vacuum or conventional dehydration methods to make the water content reach 10-50% to break the emulsion, add 60-100 ℃ hot water 1-10 times the weight of the precipitate, and use a suspension separator to separate the protein solution and oil Separate, or use a conical static separator with a heating device to heat for 1-5 hours to separate the protein solution and oil;

4、采用截留分子量为5000-100000的超滤器浓缩上述上清液和后来得到的蛋白溶液中的蛋白质,使其浓度达到1-5%后,调节其pH至2-11,采用离心或过滤的办法收集蛋白质沉淀,喷雾干燥得分离蛋白制品。4. Use an ultrafilter with a molecular weight cut-off of 5,000-100,000 to concentrate the protein in the above supernatant and the protein solution obtained later to make the concentration reach 1-5%, adjust its pH to 2-11, and use centrifugation or filtration The way to collect protein precipitates, spray-dried to isolate protein products.

本发明的优点是:成本低,蛋白质和油提取率高,同时能去掉其中的不利营养因子,所得的蛋白和油都能达到食用标准。The invention has the advantages of low cost, high protein and oil extraction rate, and can remove unfavorable nutritional factors therein, and the obtained protein and oil can all meet the edible standard.

具体实施方式:Detailed ways:

实施例1:Example 1:

称取100公斤油菜籽放入500公斤5/10000亚硫酸钠水溶液中,用一装有50目筛网的浆渣分离机磨浆除去粗纤维,重复上述步骤2次,采用离心机除尽浆中的残渣,所得的浆调节pH至5.5,用悬液分离器分离含油脂为主的沉淀部分和含有蛋白及其它水溶性物质的上清液,将沉淀进行常规脱水,使其含水量达到30%破乳,加入沉淀重量1倍的100℃热水,采用悬液分离器将蛋白溶液和油分开,用截留分子量为5000的超滤器浓缩上述上清液和后来得到的蛋白溶液中的蛋白质,使其浓度达到2%后,调整其pH至4,采用离心机收集蛋白质沉淀,喷雾干燥得分离蛋白制品。Weigh 100 kilograms of rapeseed and put it into 500 kilograms of 5/10000 sodium sulfite aqueous solution, use a pulp and residue separator equipped with a 50-mesh screen to refine the pulp to remove coarse fibers, repeat the above steps twice, and use a centrifuge to remove the pulp. Residue, the obtained slurry is adjusted to pH 5.5, and the sediment part mainly containing oil and the supernatant containing protein and other water-soluble substances are separated by a suspension separator, and the sediment is subjected to conventional dehydration to make the water content reach 30%. Milk, add hot water at 100°C that is 1 times the weight of the precipitate, use a suspension separator to separate the protein solution from the oil, and use an ultrafilter with a molecular weight cut-off of 5000 to concentrate the protein in the above supernatant and the protein solution obtained later to make After the concentration reaches 2%, the pH is adjusted to 4, the protein precipitate is collected by a centrifuge, and the isolated protein product is obtained by spray drying.

实施例2:Example 2:

称取200公斤油菜籽放入400公斤1/1000亚硫酸钠水溶液中,用一装有120目筛网的浆渣分离机磨浆除去粗纤维,重复上述步骤3次,采用离心机除尽浆中的残渣,所得的浆调节pH至2,用离心机分离含油脂为主的沉淀部分和含有蛋白及其它水溶性物质的上清液,将沉淀进行真空脱水,使其含水量达到50%破乳,加入沉淀重量5倍的80℃热水,采用锥型静止分离器加热5小时将蛋白溶液和油分开,采用截留分子量为50000的超滤浓缩上述上清液和后来得到的蛋白溶液中的蛋白质,使其浓度达到5%后,调整其pH至11,采用离心机收集蛋白质沉淀,喷雾干燥得分离蛋白制品。Weigh 200 kilograms of rapeseed and put it into 400 kilograms of 1/1000 sodium sulfite aqueous solution, use a slurry separator equipped with a 120-mesh screen to refine the pulp to remove the crude fiber, repeat the above steps 3 times, and use a centrifuge to remove the pulp. Residue, the resulting slurry is adjusted to a pH of 2, and a centrifuge is used to separate the precipitate mainly containing oil and the supernatant containing protein and other water-soluble substances, and the precipitate is vacuum dehydrated to make the water content reach 50% to break the emulsion. Add 80°C hot water five times the weight of the precipitate, and use a cone-shaped static separator to heat for 5 hours to separate the protein solution from the oil, and use ultrafiltration with a molecular weight cut-off of 50,000 to concentrate the protein in the above supernatant and the protein solution obtained later. After the concentration reaches 5%, the pH is adjusted to 11, the protein precipitate is collected by a centrifuge, and the isolated protein product is obtained by spray drying.

实施例3:Example 3:

称取200公斤油菜籽放入3000公斤的5/1000000亚硫酸钠水溶液中,用一装有200目筛网的浆渣分离机磨浆除去粗纤维,重复上述步骤3次,采用精细过滤除尽浆中的残渣,然后将所得的浆调节pH至11,用过滤器分离含油脂为主的沉淀部分和含有蛋白及其它水溶性物质的上清液,沉淀采用真空脱水,使其含水量达到10%破乳,加入沉淀重量10倍的60℃热水,采用带加热装置的锥型静止分离器加热1小时将蛋白溶液和油分开,采用截留分子量为100000的超滤器浓缩上述上清液和后来得到的蛋白溶液中的蛋白质,使其浓度达到1%后,调节其pH至6,采用离心或过滤的办法收集蛋白质沉淀,喷雾干燥得分离蛋白制品。Weigh 200 kg of rapeseed and put it into 3,000 kg of 5/1,000,000 sodium sulfite aqueous solution, use a pulp and residue separator equipped with a 200-mesh screen to remove coarse fibers, repeat the above steps 3 times, and use fine filtration to remove the pulp. Then adjust the pH of the obtained slurry to 11, use a filter to separate the precipitate mainly containing oil and the supernatant containing protein and other water-soluble substances, and vacuum dehydrate the precipitate to make its water content reach 10%. Milk, add 60 ℃ hot water 10 times the weight of the precipitate, use a conical static separator with a heating device to heat for 1 hour to separate the protein solution from the oil, use an ultrafilter with a molecular weight cut-off of 100,000 to concentrate the above supernatant and obtain After the concentration of the protein in the protein solution reaches 1%, the pH is adjusted to 6, the protein precipitate is collected by centrifugation or filtration, and the separated protein product is obtained by spray drying.

实施例4:Example 4:

称取100公斤油菜籽放入1000公斤的1/100000亚硫酸钠水溶液中,用一装有200目筛网的浆渣分离机磨浆除去粗纤维,重复上述步骤3次,采用精细过滤除尽浆中的残渣,然后将所得的浆调节pH至8,用过滤器分离含油脂为主的沉淀部分和含有蛋白及其它水溶性物质的上清液,沉淀采用真空脱水,使其含水量达到10%破乳,加入沉淀重量10倍的60℃热水,采用带加热装置的锥型静止分离器加热3小时将蛋白溶液和油分开,采用截留分子量为10000的超滤器浓缩上述上清液和后来得到的蛋白溶液中的蛋白质,使其浓度达到3%后,调节其pH至6,采用离心或过滤的办法收集蛋白质沉淀,喷雾干燥得分离蛋白制品。Weigh 100 kg of rapeseed and put it into 1,000 kg of 1/100,000 sodium sulfite aqueous solution, use a pulp and residue separator equipped with a 200-mesh screen to remove coarse fibers, repeat the above steps 3 times, and use fine filtration to remove the pulp. Then adjust the pH of the obtained slurry to 8, use a filter to separate the precipitate mainly containing oil and the supernatant containing protein and other water-soluble substances, and vacuum dehydrate the precipitate to make the water content reach 10%. Milk, add 60 ℃ hot water 10 times the weight of the precipitate, use a conical static separator with a heating device to heat for 3 hours to separate the protein solution and oil, use an ultrafilter with a molecular weight cut-off of 10,000 to concentrate the above supernatant and obtain After the protein in the protein solution reaches a concentration of 3%, its pH is adjusted to 6, and the protein precipitate is collected by centrifugation or filtration, and spray-dried to obtain an isolated protein product.

Claims (1)

1、一种水剂法生产食用菜籽蛋白和油脂的方法,其特征在于,依次包括下列步骤:1. A method for producing edible rapeseed protein and oil by water preparation, characterized in that it comprises the following steps successively: (1)将油菜籽放入其重量2-15倍的5/1000000-1/1000亚硫酸钠水溶液中,用一装有50-200目筛网的浆渣分离机磨浆除去粗纤维,重复上述步骤2-3次;(1) Put the rapeseed into 5/1000000-1/1000 sodium sulfite aqueous solution which is 2-15 times its weight, and remove the crude fiber with a slurry separator equipped with a 50-200 mesh screen, and repeat the above steps 2-3 times; (2)采用离心或精细过滤除尽浆中的残渣,然后将所得的浆调节pH至2-11,用离心机、过滤器或悬液分离器分离含油脂为主的沉淀部分和含有蛋白及其它水溶性物质的上清液;(2) Use centrifugation or fine filtration to remove the residue in the slurry, then adjust the pH of the resulting slurry to 2-11, and use a centrifuge, filter or suspension separator to separate the fat-containing precipitate and the protein-containing and Supernatants of other water-soluble substances; (3)将沉淀用真空或常规的脱水办法脱水,使其含水量达到10-50%破乳,加入沉淀重量1-10倍的60-100℃热水,采用悬液分离器将蛋白溶液和油分开,或采用带加热装置的锥型静止分离器加热1-5小时将蛋白溶液和油分开;(3) Dehydrate the precipitate with vacuum or conventional dehydration methods to make the water content reach 10-50% to break the emulsion, add 60-100°C hot water 1-10 times the weight of the precipitate, and use a suspension separator to separate the protein solution and Separate the oil, or use a conical static separator with a heating device to heat for 1-5 hours to separate the protein solution from the oil; (4)采用截留分子量为5000-100000的超滤器浓缩上述上清液和后来得到的蛋白溶液中的蛋白质,使其浓度达到1-5%后,调节其pH至2-11,采用离心或过滤的办法收集蛋白质沉淀,喷雾干燥得分离蛋白制品。(4) Concentrate the protein in the above-mentioned supernatant and the protein solution obtained later by using an ultrafilter with a molecular weight cut-off of 5000-100000, after making its concentration reach 1-5%, adjust its pH to 2-11, and use centrifugation or The protein precipitate is collected by filtration, and spray-dried to obtain the isolated protein product.
CNB021038074A 2002-03-27 2002-03-27 Method for producing edible rapeseed protein and oil by aqueous method Expired - Fee Related CN1177024C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB021038074A CN1177024C (en) 2002-03-27 2002-03-27 Method for producing edible rapeseed protein and oil by aqueous method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB021038074A CN1177024C (en) 2002-03-27 2002-03-27 Method for producing edible rapeseed protein and oil by aqueous method

Publications (2)

Publication Number Publication Date
CN1374383A CN1374383A (en) 2002-10-16
CN1177024C true CN1177024C (en) 2004-11-24

Family

ID=4739905

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB021038074A Expired - Fee Related CN1177024C (en) 2002-03-27 2002-03-27 Method for producing edible rapeseed protein and oil by aqueous method

Country Status (1)

Country Link
CN (1) CN1177024C (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101160579B1 (en) * 2003-06-20 2012-06-28 버콘 뉴트라사이언스 (엠비) 코포레이션 Oil seed meal preparation
WO2007068143A1 (en) * 2005-12-13 2007-06-21 Lanqin Yang Preparation of plant oil, crude protein and fiber by water extraction
AU2011261455B2 (en) 2010-06-01 2016-03-24 Dsm Ip Assets B.V. Extraction of lipid from cells and products therefrom
CN102250679A (en) * 2011-06-09 2011-11-23 安徽中草香料有限公司 Preparation process for fragrant vegetable seed oil
ES2909791T3 (en) 2013-12-20 2022-05-10 Dsm Ip Assets Bv Processes to obtain microbial oil from microbial cells
AR098895A1 (en) 2013-12-20 2016-06-22 Dsm Ip Assets Bv PROCESS FOR OBTAINING MICROBIAL OIL FROM MICROBIAL CELLS
TWI698520B (en) 2013-12-20 2020-07-11 荷蘭商Dsm智慧財產有限公司 Processes for obtaining microbial oil from microbial cells
JP2017501709A (en) 2013-12-20 2017-01-19 ディーエスエム アイピー アセッツ ビー.ブイ. Method for obtaining microbial oil from microbial cells
CA2934490C (en) 2013-12-20 2022-05-03 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells
CN110432333A (en) * 2019-08-30 2019-11-12 黑龙江省上草堂野生荭菇娘研究开发有限公司 A kind of groundcherry Calyx Physalis seed hypoglycemic polysaccharide protein reconstitutes the preparation method of product

Also Published As

Publication number Publication date
CN1374383A (en) 2002-10-16

Similar Documents

Publication Publication Date Title
US4889921A (en) Production of rapeseed protein materials
US7645468B2 (en) Oil seed meal preparation
CA1068542A (en) Process for preparation of fish meat extracts
AU2002339797B2 (en) Process for the fractionation of oilseed press cakes and meals
EP2285824B1 (en) Production of protein isolates
CN1177024C (en) Method for producing edible rapeseed protein and oil by aqueous method
DE2723940A1 (en) METHOD OF TREATMENT OF CORN HELLS
EP1446022A1 (en) Oilseed processing
CN111499771A (en) A method for simultaneously extracting oil, protein and polysaccharide in rice bran by three-phase extraction technology
CN101297689A (en) Pure natural edible fresh chili oil and preparation thereof
CN107847891A (en) The method that saponin(e is extracted from agricultural product
US6602985B1 (en) Extraction of zein protein from gluten meal
US4151310A (en) Soybean protein extract
TWI756203B (en) Preparation of non-soy oilseed protein products (“*810”)
US4018936A (en) Gluten treatment
JP2021529546A (en) How to Prepare Protein-Fiber Concentrates from Plant Materials
WO2007119694A1 (en) Method for processing squeezed residue of palm fruit and/or mesocarp thereof
CA2653743C (en) Process for aqueous oil extraction from oilseed starting material
SU1275032A1 (en) Method of producing sea buckthorn oil from press
CN111528335B (en) Method for preparing high-protein-content linseed protein by aqueous medium method
US1808737A (en) Method of producing citrus fruit products
RU2815553C1 (en) Method of producing protein isolate from rapeseed cake
RU2852692C1 (en) Method for isolating food-grade astaxanthin-containing protein hydrolysate
US20250019734A1 (en) Process for obtaining proteins from hemp
CN1349755A (en) Edible protein producing process with plant leaf

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee

Owner name: SOUTHWEST UNIVERSITY

Free format text: FORMER NAME: SOUTHWEST AGRICULTURAL UNIVERSITY

CP01 Change in the name or title of a patent holder

Address after: 400716 No. 216, natural road, Beibei District, Chongqing

Patentee after: Southwest University

Address before: 400716 No. 216, natural road, Beibei District, Chongqing

Patentee before: Southwest Agricultural University

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20041124

Termination date: 20130327