CN1837177A - Process for preparing alpha-zinc linolenate - Google Patents

Process for preparing alpha-zinc linolenate Download PDF

Info

Publication number
CN1837177A
CN1837177A CN 200510107354 CN200510107354A CN1837177A CN 1837177 A CN1837177 A CN 1837177A CN 200510107354 CN200510107354 CN 200510107354 CN 200510107354 A CN200510107354 A CN 200510107354A CN 1837177 A CN1837177 A CN 1837177A
Authority
CN
China
Prior art keywords
linolenic acid
zinc
alpha
solution
container
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
CN 200510107354
Other languages
Chinese (zh)
Other versions
CN100363324C (en
Inventor
宋宪生
张金阳
崔卫民
宋军
张群峰
张辉
张拥强
杨坡
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.)
He'nan Linuo Bio-chemistry Co., Ltd.
Taiyuan Haicheng Biomedical Technology Co.,Ltd.
Original Assignee
ANYANG CHEMICAL INDUSTRY GROUP Co Ltd
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 ANYANG CHEMICAL INDUSTRY GROUP Co Ltd filed Critical ANYANG CHEMICAL INDUSTRY GROUP Co Ltd
Priority to CNB2005101073547A priority Critical patent/CN100363324C/en
Publication of CN1837177A publication Critical patent/CN1837177A/en
Application granted granted Critical
Publication of CN100363324C publication Critical patent/CN100363324C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention relates to a process for preparing alpha-zinc linolenate by using perilla oil as the raw material, which comprises the steps of saponifying, neutralizing, double decomposition, stewing, scouring, dewatering and drying. The obtained alpha-zinc linolenate has higher content of alpha-linolenic acid.

Description

The preparation method of alpha-linolenic acid zinc
Technical field
The present invention relates to a kind of is the preparation method of raw material production alpha-linolenic acid zinc with the perilla oil.
Background technology
Alpha-linolenic acid mainly is present in the various plants grease with the triglyceride level form, comprise linseed oil, Purple Perilla Seed Oil, rape seed oil, Oleum Gossypii semen, soybean wet goods, wherein content is up to 50%~60% in linseed oil, the Purple Perilla Seed Oil, and content is all below 10% in other oil.To unsaturated fatty acids famine, particularly alpha-linolenic acid, need to replenish among the crowd from other approach.In medicine, food service industry, how to use, generally lack zinc in addition among the crowd, make the combination of alpha-linolenic acid and zinc, make the crowd replenish alpha-linolenic acid and zinc preferably as adding, and the domestic present not preparation method of invention alpha-linolenic acid zinc.
Summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art and the preparation method of the also big alpha-linolenic acid zinc of a kind of content that not only contains a large amount of alpha-linolenic acids and zinc is provided.
The object of the present invention is achieved like this: carry out according to following technology:
The first step: saponification: perilla oil and the deionized water ratio by weight 1: 0.5~4 is added in the container; stir and heating, control material reaction temperature slowly adds 5%~30% ionic membrane caustic soda between 40 ℃~90 ℃; when the material pH value greater than 12 the time; stop to add ionic membrane caustic soda, when the material pH value less than 10 the time, slowly add ionic membrane caustic soda; when the material pH value keeps 2 hours when constant greater than 10; reaction finishes, the omnidistance logical nitrogen protection of this operation
Second step: neutralization: add in container and stirring in 1: 3~10 ratio the first step gained material, deionized water weight ratio; obtain milky white solution, slowly add 30%~90% sulfuric acid milky white solution is neutralized to PH=7, this operation finishes; the omnidistance logical nitrogen protection of this operation
The 3rd step: metathesis: zinc sulfate, deionized water are configured to solution of zinc sulfate by weight 1: 4~10 ratio adding container and stirring; the second step gained material and solution of zinc sulfate are added in the container; control reaction temperature is between 40 ℃~90 ℃; stir; 1~3 hour time can produce a large amount of dispersive white floss---alpha-linolenic acid zinc, and this operation finishes; the omnidistance logical nitrogen protection of this operation
The 4th step: leave standstill: the 3rd step gained material is left standstill in container, and temperature is controlled between 40~90 ℃, left standstill 6~10 hours,
The 5th step: washing: discharge the aqueous solution in the 4th step gained material, add deionized water white alpha-linolenic acid zinc floss is washed, drainage water solution repeats aforesaid operations, and is as clear as crystal until the aqueous solution of discharging,
The 6th step: dehydration: the 5th step gained material is put into whizzer, carry out centrifuge dehydration, make alpha-linolenic acid zinc and water realize solid-liquid separation,
The 7th step: drying:, promptly get little yellow solid alpha-linolenic acid zinc with the 6th step gained solid materials under 40~90 ℃, vacuum 400~700mmHg condition dry 20~35 hours.
The present invention has following positively effect:
The first, the present invention has successfully realized the preparation of alpha-linolenic acid zinc.
The second, make the interpolation approach of alpha-linolenic acid more extensive.
Three, make the crowd better replenish alpha-linolenic acid and zinc, promoted that effectively the crowd is healthy.
Four, the alpha-linolenic acid content height of the alpha-linolenic acid zinc of the present invention's preparation, alpha-linolenic acid content is greater than 55%, and the content of zinc is greater than 6%, and all other indexs meet the provisions of the relevant regulations issued by the State.
Embodiment
Embodiment 1:
The first step: saponification: perilla oil 100 grams and deionized water 50 grams are added in the container; stir and heating, 40 ℃ of control material reaction temperature slowly add 5% ionic membrane caustic soda; when the material pH value greater than 12 the time; stop to add ionic membrane caustic soda, when the material pH value less than 10 the time, slowly add ionic membrane caustic soda; keep greater than 10 when the material pH value and to keep 2 hours when constant; reaction finishes, the omnidistance logical nitrogen protection of this operation
Second step: neutralize: add in the containers the first step gained material 450 grams, deionized water 1350 grams and stirring, obtain milky white solution, slowly add 30% sulfuric acid milky white solution is neutralized to PH=7, this operation finishes, the omnidistance logical nitrogen protection of this operation,
The 3rd step: metathesis: be configured to solution of zinc sulfate with also stirring in zinc sulfate 100 grams, the deionized water 400 gram adding containers; the second step gained material and solution of zinc sulfate are added in the container; 40 ℃ of control reaction temperature; stir; 1 hour time can produce a large amount of dispersive white floss---alpha-linolenic acid zinc, and this operation finishes; the omnidistance logical nitrogen protection of this operation
The 4th step: leave standstill: the 3rd step gained material is left standstill in container, and 40 ℃ of temperature controls were left standstill 6 hours,
The 5th step: washing: discharge the aqueous solution in the 4th step gained material, add deionized water white alpha-linolenic acid zinc floss is washed, drainage water solution repeats aforesaid operations, and is as clear as crystal until the aqueous solution of discharging,
The 6th step: dehydration: the 5th step gained material is put into whizzer, carry out centrifuge dehydration, make alpha-linolenic acid zinc and water realize solid-liquid separation,
The 7th step: drying:, promptly get little yellow solid alpha-linolenic acid zinc 5 and restrain with the 6th step gained solid materials under 40 ℃, vacuum 400mmHg condition dry 20 hours.
Embodiment 2:
The first step: saponification: perilla oil 100 grams and deionized water 400 grams are added in the container; stir and heating, 90 ℃ of control material reaction temperature slowly add 30% ionic membrane caustic soda; when the material pH value greater than 12 the time; stop to add ionic membrane caustic soda, when the material pH value less than 10 the time, slowly add ionic membrane caustic soda; when the material pH value keeps 2 hours when constant greater than 10; reaction finishes, the omnidistance logical nitrogen protection of this operation
Second step: neutralize: add in the containers the first step gained material 600 grams, deionized water 6000 grams and stirring, obtain milky white solution, slowly add 90% sulfuric acid milky white solution is neutralized to PH=7, this operation finishes, the omnidistance logical nitrogen protection of this operation,
The 3rd step: metathesis: be configured to solution of zinc sulfate with also stirring in zinc sulfate 100 grams, the deionized water 1000 gram adding containers; the second step gained material and solution of zinc sulfate are added in the container; 90 ℃ of control reaction temperature; stir; 3 hours time can produce a large amount of dispersive white floss---alpha-linolenic acid zinc, and this operation finishes; the omnidistance logical nitrogen protection of this operation
The 4th step: leave standstill: the 3rd step gained material is left standstill in container, and 90 ℃ of temperature controls were left standstill 10 hours,
The 5th step: washing: discharge the aqueous solution in the 4th step gained material, add deionized water white alpha-linolenic acid zinc floss is washed, drainage water solution repeats aforesaid operations, and is as clear as crystal until the aqueous solution of discharging,
The 6th step: dehydration: the 5th step gained material is put into whizzer, carry out centrifuge dehydration, make alpha-linolenic acid zinc and water realize solid-liquid separation,
The 7th step: drying:, promptly get little yellow solid alpha-linolenic acid zinc 6 and restrain with the 6th step gained solid materials under 90 ℃, vacuum 700mmHg condition dry 35 hours.
Embodiment 3:
The first step: saponification: perilla oil 100 grams and deionized water 200 grams are added in the container; stir and heating, 60 ℃ of control material reaction temperature slowly add 20% ionic membrane caustic soda; when the material pH value greater than 12 the time; stop to add ionic membrane caustic soda, when the material pH value less than 10 the time, slowly add ionic membrane caustic soda; keep greater than 10 when the material pH value and to keep 2 hours when constant; reaction finishes, the omnidistance logical nitrogen protection of this operation
Second step: neutralization: the first step gained material 380, deionized water 1900 are restrained to add in the containers and also stir, obtain milky white solution, slowly add 80% sulfuric acid milky white solution is neutralized to PH=7, this operation finishes, the logical nitrogen protection of this operation whole process,
The 3rd step: metathesis; Be configured to solution of zinc sulfate with also stirring in zinc sulfate 100 grams, the deionized water 500 gram adding containers; the second step gained material and solution of zinc sulfate are added in the container; between 80 ℃ of the control reaction temperature; stir; 2 hours time can produce a large amount of dispersive white floss---alpha-linolenic acid zinc, and this operation finishes; the omnidistance logical nitrogen protection of this operation
The 4th step: leave standstill: the 3rd step gained material is left standstill in container, and 50 ℃ of temperature controls were left standstill 8 hours,
The 5th step: washing: discharge the aqueous solution in the 4th step gained material, add deionized water white alpha-linolenic acid zinc floss is washed, drainage water solution repeats aforesaid operations, and is as clear as crystal until the aqueous solution of discharging,
The 6th step: dehydration: the 5th step gained material is put into whizzer, carry out centrifuge dehydration, make alpha-linolenic acid zinc and water realize solid-liquid separation,
The 7th step: drying:, promptly get little yellow solid alpha-linolenic acid zinc 5 and restrain with the 6th step gained solid materials under 60 ℃, vacuum 500mmHg condition dry 25 hours.

Claims (1)

1, a kind of preparation method of alpha-linolenic acid calcium zinc is characterized in that: carry out according to following technology:
The first step: saponification: perilla oil and the deionized water ratio by weight 1: 0.5~4 is added in the container; stir and heating, control material reaction temperature slowly adds 5%~30% ionic membrane caustic soda between 40 ℃~90 ℃; when the material pH value greater than 12 the time; stop to add ionic membrane caustic soda, when the material pH value less than 10 the time, slowly add ionic membrane caustic soda; when the material pH value greater than 10 and keep 2 hours when constant; reaction finishes, the omnidistance logical nitrogen protection of this operation
Second step: neutralization: the first step gained material, deionized water are also stirred in 1: 3~10 ratio adding container; obtain milky white solution, slowly add 30%~90% sulfuric acid milky white solution is neutralized to PH=7, this operation finishes; the omnidistance logical nitrogen protection of this operation
The 3rd step: metathesis: zinc sulfate, deionized water are configured to solution of zinc sulfate by weight 1: 4~10 ratio adding container and stirring; the second step gained material and solution of zinc sulfate are added in the container; control reaction temperature is between 40 ℃~90 ℃; stir; 1~3 hour time produced a large amount of dispersive white floss---linolenic acid zinc, and this operation finishes; the omnidistance logical nitrogen protection of this operation
The 4th step: leave standstill: the 3rd step gained material is left standstill in container, and temperature is controlled between 40~90 ℃, left standstill 6~10 hours,
The 5th step: washing: discharge the aqueous solution in the 4th step gained material, add deionized water white linolenic acid zinc floss is washed, drainage water solution repeats aforesaid operations, and is as clear as crystal until the aqueous solution of discharging,
The 6th step: dehydration: the 5th step gained material is put into whizzer, carry out centrifuge dehydration, make linolenic acid zinc and water realize solid-liquid separation,
The 7th step: drying:, promptly get solid alpha-linolenic acid zinc with the 6th step gained solid materials under 40~90 ℃, vacuum 400~700mmHg condition dry 20~35 hours.
CNB2005101073547A 2005-12-30 2005-12-30 Process for preparing alpha-zinc linolenate Expired - Fee Related CN100363324C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2005101073547A CN100363324C (en) 2005-12-30 2005-12-30 Process for preparing alpha-zinc linolenate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2005101073547A CN100363324C (en) 2005-12-30 2005-12-30 Process for preparing alpha-zinc linolenate

Publications (2)

Publication Number Publication Date
CN1837177A true CN1837177A (en) 2006-09-27
CN100363324C CN100363324C (en) 2008-01-23

Family

ID=37014708

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2005101073547A Expired - Fee Related CN100363324C (en) 2005-12-30 2005-12-30 Process for preparing alpha-zinc linolenate

Country Status (1)

Country Link
CN (1) CN100363324C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108623448A (en) * 2018-05-15 2018-10-09 南京医科大学 The preparation of leukotrienes zinc and its application in preparing Anti-helicobacter pylori drugs

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1098072C (en) * 1998-05-12 2003-01-08 李文光 Medicinal products of superfined alpha-linolenic acid, preparing process and preparation thereof
CN1270160A (en) * 1999-04-14 2000-10-18 李文光 Refined unsaturated polyfatty acid and calcium salt of unsaturated polyfatty acid as medicinal products and preparing process thereof and preparation

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108623448A (en) * 2018-05-15 2018-10-09 南京医科大学 The preparation of leukotrienes zinc and its application in preparing Anti-helicobacter pylori drugs
WO2019219093A3 (en) * 2018-05-15 2019-12-19 南京医科大学 Preparation of zinc linoleate, and application thereof in preparing anti-helicobacter pylori drug
US11203563B2 (en) 2018-05-15 2021-12-21 Nanjing Medical University Preparation of zinc linolenate, and application of zinc linolenate in preparing anti-helicobacter pylori drug

Also Published As

Publication number Publication date
CN100363324C (en) 2008-01-23

Similar Documents

Publication Publication Date Title
US9546342B1 (en) Complete saponification and acidulation of natural oil processing byproducts
CN102965182B (en) Method for extracting grease from schizochytrium
CN109574826B (en) Preparation method of high-purity oleic acid
RU2015122025A (en) Methods and apparatus for the production of nanocellulose and compositions and products derived from it
DE2134215C3 (en) Process for the production of detergents and cleaning agents
CN110669254B (en) Method for preparing epoxy plasticizer from waste grease
SE540045C2 (en) Method of producing lignin with reduced amount of odorous substances, lignin product obtained by the method and use of the lignin product
CN113024376B (en) Production process of hexadecanediester
CN101747997B (en) Method for preparing monolaurin
CN1837179A (en) Process for preparing alpha-linolenic acid with purity more than 80%
CN1837178A (en) Process for preparing alpha-calcium linolenate
CN1837177A (en) Process for preparing alpha-zinc linolenate
CN108164407A (en) A kind of method that aqueous phase oxidation biomass prepares single phenol, small molecular organic acid and high purity cellulose
SG174443A1 (en) Method for producing polymeric solids
CN106753753A (en) The extraction process of fatty acid mixed in a kind of vegetable oil residue
CN101831356A (en) Method for preparing linseed oil fatty acid with light color
DE2025238B2 (en) Powdered detergents and cleaning agents
CN112521324A (en) Preparation method of di-tert-butyl peroxide
CN111410916A (en) Preparation method of drier in white paint
CN102220185A (en) Method for simultaneously decoloring, degumming and deacidifying to refine vegetable oil
CN1904014A (en) Method of preparing fatty acid ester
CN101392148B (en) Tall oil recovery method
CN101643495B (en) Method for extracting plant sterol from fatty acid or methyl ester pitch from distillate
CN1089314C (en) Preparation of activated clay
CN111500195A (en) Preparation method of drier for preventing surface skinning

Legal Events

Date Code Title Description
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
ASS Succession or assignment of patent right

Owner name: TAIYUAN HAICHENG BIO-PHARMACEUTICAL TECHNOLOGY CO.

Owner name: HE NAN LINUO BIO-CHEMISTRY CO., LTD.

Free format text: FORMER OWNER: ANYANG CHEMICAL IDUSTRY GROUP CO., LTD.

Effective date: 20101227

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 455133 ZHANGJIAZHUANG, LONG AN DISTRICT, ANYANG CITY, HE NAN PROVINCE TO: 450000 INSIDE OF VENTURE CENTER, MIDDLE SECTION OF HAIHE AVENUE, NEW AND HIGH TECHNOLOGY DEVELOPMENT AREA, ANYANG, HE NAN PROVINCE

TR01 Transfer of patent right

Effective date of registration: 20101227

Address after: 450000 Henan Anyang hi tech Development Zone Haihe road middle Venture Center Hospital

Co-patentee after: Taiyuan Haicheng Biomedical Technology Co.,Ltd.

Patentee after: He'nan Linuo Bio-chemistry Co., Ltd.

Address before: Long'an District Anyang city of Henan Province Zhang Jia Zhuang 455133

Patentee before: Anyang Chemical Industry Group Co., Ltd.

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

Granted publication date: 20080123

Termination date: 20111230