CN101037455A - Method for extracting raffinose from cottonseed meal - Google Patents

Method for extracting raffinose from cottonseed meal Download PDF

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Publication number
CN101037455A
CN101037455A CN 200710014172 CN200710014172A CN101037455A CN 101037455 A CN101037455 A CN 101037455A CN 200710014172 CN200710014172 CN 200710014172 CN 200710014172 A CN200710014172 A CN 200710014172A CN 101037455 A CN101037455 A CN 101037455A
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China
Prior art keywords
raffinose
cottonseed
cotton
cotton dregs
gets
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Pending
Application number
CN 200710014172
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Chinese (zh)
Inventor
孙宁祥
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.)
Zhongmian Ziguang Biological Science And Technology Co Ltd Beijing
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Individual
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 Individual filed Critical Individual
Priority to CN 200710014172 priority Critical patent/CN101037455A/en
Publication of CN101037455A publication Critical patent/CN101037455A/en
Priority to CN2008100896362A priority patent/CN101265280B/en
Pending legal-status Critical Current

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Abstract

The invention relates to a method for extracting raffinose from cottonseed meal, including following steps: removing the cottonseed rind to get cottonseed kernel, softing the embryo of the cottonseed kernel, dipping the cottonseed oil with solvent-extracted oil, getting cotton dregs; adding 40-100wt.% of carbinol in the cotton dregs, dipping for 20-60 minutes at 0-70 DEG C, after removing the carbinol, getting coarse raffinose; dissolving the coarse raffinose by water or rare acid, controlling temperature at 0-100 DEG C, pH=2-7, filtering, decoloring, concentrating, crystallize, drying, getting extractive raffinose. The invention re-exacts the raffinose after degreasing, ensures to attain the raffinose as well as perfect conttonseed oil, and reduces the dissociative gossypol content in the cotton dregs and improves the cotton dreg quality.

Description

A kind of method of in cottonseed meal, extracting raffinose
(1) technical field
The invention discloses a kind of preparation method of raffinose, particularly a kind of method of in cottonseed meal, extracting raffinose.
(2) background technology
Existing cotton dregs generally only extract Oleum Gossypii semen, and raffinose, the gossypol of part arranged in the cotton dregs, and the cotton dregs quality is not high.
(3) summary of the invention
The present invention provides a kind of method of extracting raffinose in cottonseed meal in order to overcome the deficiency of above technology, and the one, extracted useful material raffinose, the 2nd, removed deleterious gossypol, improved the quality of cotton dregs.
The present invention realizes by following measure:
The present invention relates to a kind of method of in cottonseed meal, extracting raffinose, it is characterized in that adopting following steps:
(1) get cotton benevolence after cottonseed is peeled off, cotton benevolence is softening rolls embryo, leaches Oleum Gossypii semen with solvent oil, gets cotton dregs;
(2) adding concentration expressed in percentage by weight in the cotton dregs is the methyl alcohol of 40-100%, and leaching is 20-60 minute under 0-70 ℃ of condition, behind the separating methanol, gets the raffinose coarse fodder;
(3) raffinose coarse fodder water or diluted acid dissolve, and controlled temperature 0-100 ℃, PH=2-7 filters, and decolouring concentrates, crystallization, and oven dry gets the elaboration raffinose.
The method of the extraction raffinose of the invention described above, the concentration of described methyl alcohol are 85-98%, and leaching temperature is 40-60 ℃, and leaching time is 20-40 minute.
Operational path is as follows:
The clear seed of high-quality cottonseed-wind-force-peel off-screen-cotton benevolence-soften-rolling embryo-oven dry-6# solvent oil leaching Oleum Gossypii semen-methanol solution leaches raffinose-separating methanol-raffinose coarse fodder-dissolving-cooling-filtration-raffinose solution-decolouring-concentrated-crystallization-oven dry-crushing packing-elaboration raffinose.
The invention has the beneficial effects as follows, carry raffinose after the first degreasing again, obtain raffinose when guaranteeing to obtain high-quality cottonseed oil, and reduce the content of free gossypol in the cotton dregs, improve the quality of cotton dregs.
(4) description of drawings
Fig. 1 is pretreatment technology flow line figure of the present invention
Fig. 2 is extract technology flow line figure of the present invention
(5) embodiment
With the case of handling 150 tons of high-quality cottonseeds day extracting method of the present invention is made specific description below.
The Oleum Gossypii semen yield is 15-20%, and dephenolize cotton dregs yield is 37-42%, and raffinose coarse fodder yield is 0.5-1.0%, elaboration raffinose yield 0.3-0.8%.
Per diem handle 150 tons of high-quality cottonseeds, get Oleum Gossypii semen 22.5-30 ton, get dephenolize cotton dregs 55.5-63 ton, get raffinose coarse fodder 0.75-1.50 ton, get elaboration raffinose 0.45-1.2 ton
Extraction step is divided into the pre-treatment of cottonseed, leaches, and is refining.
One. pre-treatment
Technical process as shown in Figure 1, pretreated Technology requires as follows:
1. contain assorted≤0.5% after the cottonseed cleaning, cottonseed is got a foothold and is contained oil plant≤0.5%
2. after cottonseed is peeled off and is separated, rate of kernel in hull≤1%, rate of hull in kernel≤10%, fines content require few as far as possible.
3. softening:
Softening time 20-30 minute
Softening temperature≤80 ℃
Softening moisture 9-11%
4. strip plate
Embryo sheet thickness 0.3mm-0.4mm requires embryo sheet thickness even, solid, becomes powder few, holds and sends out pine, looses one's grip and disperses.
5. oven dry
Drying time 30 minutes
Material temperature≤80 ℃
Water content (going into immersion divides) 5-7%
Fines content is crossed 30 mesh sieves≤8%
Two. leach
Technical process as shown in Figure 2, it is as follows that Technology requires:
(1) buffer bin
Material stock height 〉=0.5 meter
(2) sealing auger
Play the effective closure effect when requiring material to enter leacher, overflow from opening for feed to prevent leacher internal solvent gas.
(3) Oleum Gossypii semen leacher
50-55 ℃ of leacher temperature, solvent temperature 50-55 ℃.
Bed thickness 〉=300mm
120 minutes running periods
Solvent and material embryo ratio: under the normal feed state, solvent ratio is 1: 0.8-1.2, miscella concentration 20%
The little negative pressure of leacher pressure
(4) raffinose gossypol leacher: it is the methyl alcohol of 85%-85% that solvent adopts concentration expressed in percentage by weight.
40-60 ℃ of leacher temperature
Solvent temperature 40-60 ℃
Material was the effective soak time of each leacher 25 minutes.
Solvent and material ratio: under the normal feed state, fresh solvent magnitude of recruitment 1-2m3/h.
(5) thickening temperature 95-105 ℃
Three. refining
Technical process:
Raffinose coarse fodder-dissolving-cooling-filtration-raffinose solution-decolouring-concentrate-crystallization-oven dry-crushing packing-elaboration raffinose.
Technology requires:
(1) solvent temperature: 60 ℃, PH=5
(2) cooling temperature≤40 ℃
(3) raffinose elaboration operative norm Q/HDCCU009-2006.

Claims (2)

1. method of extracting raffinose in cottonseed meal is characterized in that adopting following steps:
(1) get cotton benevolence after cottonseed is peeled off, cotton benevolence is softening rolls embryo, leaches Oleum Gossypii semen with solvent oil, gets cotton dregs;
(2) adding concentration expressed in percentage by weight in the cotton dregs is the methyl alcohol of 40-100%, and leaching is 20-60 minute under 0-70 ℃ of condition, behind the separating methanol, gets the raffinose coarse fodder;
(3) raffinose coarse fodder water or diluted acid dissolve, and controlled temperature 0-100 ℃, PH=2-7 filters, and decolouring concentrates, crystallization, and oven dry gets the elaboration raffinose.
2. plant according to power and require 1 described method, it is characterized in that the concentration of described methyl alcohol is 85-98%, leaching temperature is 40-60 ℃, and leaching time is 20-40 minute.
CN 200710014172 2007-04-13 2007-04-13 Method for extracting raffinose from cottonseed meal Pending CN101037455A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN 200710014172 CN101037455A (en) 2007-04-13 2007-04-13 Method for extracting raffinose from cottonseed meal
CN2008100896362A CN101265280B (en) 2007-04-13 2008-04-11 Method for extracting raffinose from cottonseed scum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200710014172 CN101037455A (en) 2007-04-13 2007-04-13 Method for extracting raffinose from cottonseed meal

Publications (1)

Publication Number Publication Date
CN101037455A true CN101037455A (en) 2007-09-19

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CN 200710014172 Pending CN101037455A (en) 2007-04-13 2007-04-13 Method for extracting raffinose from cottonseed meal
CN2008100896362A Expired - Fee Related CN101265280B (en) 2007-04-13 2008-04-11 Method for extracting raffinose from cottonseed scum

Family Applications After (1)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102351917A (en) * 2011-09-14 2012-02-15 北京科技大学 Method for extracting raffinose from cotton seed meal
CN101785527B (en) * 2009-12-22 2012-09-26 晨光生物科技集团股份有限公司 Method for preparing dephenolization cottonseed protein and raffinose
CN102898486A (en) * 2012-09-21 2013-01-30 晨光生物科技集团股份有限公司 Comprehensive method for preparation of raffinose and gossypol from cottonseed meal
CN103819514A (en) * 2014-01-23 2014-05-28 新疆农垦科学院 Cotton seed meal dephenolizing technology and method for preparing raffinose from cotton seed meal by technology
CN106967129A (en) * 2017-03-24 2017-07-21 合肥云都棉花有限公司 A kind of extracting method of raffinose
CN107056850A (en) * 2017-03-24 2017-08-18 合肥云都棉花有限公司 A kind of method that raffinose is extracted from cottonseed

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101367846B (en) * 2008-09-27 2010-12-22 浙江大学 Percolation extraction method for raffinose
CN101367845B (en) * 2008-09-27 2010-12-22 浙江大学 Decolorization method for raffinose raffinate
CN102070677B (en) * 2011-01-28 2012-12-19 湖南省丰康生物科技股份有限公司 Method for refining raffinose
CN106380494B (en) * 2016-08-19 2019-07-12 晨光生物科技集团喀什有限公司 A kind of raffinose production technology of crude
CN110833115A (en) * 2019-11-21 2020-02-25 南京胜昔实业有限公司 Comprehensive utilization method of cotton production by-products by using biochemical fulvic acid as main product

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101785527B (en) * 2009-12-22 2012-09-26 晨光生物科技集团股份有限公司 Method for preparing dephenolization cottonseed protein and raffinose
CN102351917A (en) * 2011-09-14 2012-02-15 北京科技大学 Method for extracting raffinose from cotton seed meal
CN102898486A (en) * 2012-09-21 2013-01-30 晨光生物科技集团股份有限公司 Comprehensive method for preparation of raffinose and gossypol from cottonseed meal
CN102898486B (en) * 2012-09-21 2015-07-22 晨光生物科技集团股份有限公司 Comprehensive method for preparation of raffinose and gossypol from cottonseed meal
CN103819514A (en) * 2014-01-23 2014-05-28 新疆农垦科学院 Cotton seed meal dephenolizing technology and method for preparing raffinose from cotton seed meal by technology
CN103819514B (en) * 2014-01-23 2016-04-06 新疆农垦科学院 Cotton dregs dephenolize technology and utilize this technology to prepare the method for raffinose from cotton dregs
CN106967129A (en) * 2017-03-24 2017-07-21 合肥云都棉花有限公司 A kind of extracting method of raffinose
CN107056850A (en) * 2017-03-24 2017-08-18 合肥云都棉花有限公司 A kind of method that raffinose is extracted from cottonseed

Also Published As

Publication number Publication date
CN101265280A (en) 2008-09-17
CN101265280B (en) 2011-12-07

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