CN108841443A - A kind of refined rice bran oil combination degumming alkali refining method - Google Patents
A kind of refined rice bran oil combination degumming alkali refining method Download PDFInfo
- Publication number
- CN108841443A CN108841443A CN201810671157.5A CN201810671157A CN108841443A CN 108841443 A CN108841443 A CN 108841443A CN 201810671157 A CN201810671157 A CN 201810671157A CN 108841443 A CN108841443 A CN 108841443A
- Authority
- CN
- China
- Prior art keywords
- rice bran
- oil
- salt water
- sodium hydroxide
- phosphoric acid
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/001—Refining fats or fatty oils by a combination of two or more of the means hereafter
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS OR COOKING OILS
- A23D9/00—Other edible oils or fats, e.g. shortenings or cooking oils
- A23D9/02—Other edible oils or fats, e.g. shortenings or cooking oils characterised by the production or working-up
- A23D9/04—Working-up
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/02—Refining fats or fatty oils by chemical reaction
- C11B3/04—Refining fats or fatty oils by chemical reaction with acids
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/02—Refining fats or fatty oils by chemical reaction
- C11B3/06—Refining fats or fatty oils by chemical reaction with bases
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Microbiology (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Fats And Perfumes (AREA)
Abstract
The present invention relates to oil processing field, specifically a kind of refined rice bran oil combination degumming alkali refining method, specific step is as follows:(1) oil stirring is thrown;(2) steam heats;(3) add phosphoric acid;(4) adding sodium hydroxide;(5) heating reaction;(6) add salt water;(7) stratification;(8) salt water secondary cleaning;Combine purification Rice bran crude oil with sodium hydroxide using phosphoric acid, physically method of refining simplifies technique, and equipment investment is low, and environmentally friendly, refining effect is good;Twice using salt water cleaning, the cleaning inside Rice bran crude oil has been ensured, purity is high.
Description
Technical field
The present invention relates to oil processing field, specifically a kind of refined rice bran oil combination degumming alkali refining method.
Background technique
Beating the oil chaff that rice comes out can extract oil, this is just rice bran oil, and rice bran oil is the pair as obtained in paddy processing process
Product rice bran, a kind of Rice oil produced with squeezing method or lixiviation process, private refining rice bran oil tech is also immature at present, Japan
Sensational rice bran oil poisoning once occurred, nine divisions of China in remote antiquity one, the field great Mu city Grain Processing Corporation eats oilmill, in life
When producing rice bran oil, in order to reduce cost profit-push, low price degumming raw material is used in scouring processes, degumming effect difference is held simultaneously
It easily causes harm to the human body, as the raising and people of China's rice intensive processing industry integral level are to the battalion of oils product
The attention of health-care effect is supported, the industrial chain of rice bran oil is gradually forming, and market potential will gradually discharge, and have certain production capacity
The enterprise of scale can obtain rapidly the larger market share by technical advantage, but it is safe and non-toxic be still need the step of pursuing with
Method.
Summary of the invention
To solve the above-mentioned problems, the present invention proposes a kind of refined rice bran oil combination degumming alkali refining method.
A kind of refined rice bran oil combination degumming alkali refining method, specific step is as follows:
(1) oil stirring is thrown:By in 10 tons of Rice bran crude oil investment alkali refining tank, start uniform stirring;
(2) steam heats:Steam is opened to Rice bran crude oil and is heated to 70 DEG C;
(3) add phosphoric acid:Diluted phosphoric acid is added in Rice bran crude oil and is quickly stirred to react 15 minutes;
(4) adding sodium hydroxide:Sodium hydroxide needed for free fatty acid is totally removed is calculated according to the acid value of Rice bran crude oil
30% sodium hydroxide solution is added in amount;
(5) heating reaction:Rice bran oil is warming up to 80 DEG C, is reacted 5 minutes;
(6) add salt water:Salt water and the stirring of 500 liter of 10% concentration are added in rice bran oil, it is seen that after crystalline particle, immediately
Stop stirring;
(7) stratification:By rice bran oil stratification 6 hours or more, lower layer's soap stock is released;
(8) salt water secondary cleaning:Rice bran oil is washed two times with the salt water of oil mass 5%, soap stock is released, obtains edible vegetable oil.
The amount of sodium hydroxide in the step (3) needs to remove itself acid value, and the phosphoric acid is to have in 50 liters
30% concentration, the temperature of Rice bran crude oil is maintained at 70 DEG C when the described addition phosphoric acid.
Salt water in the step (6) is 10% concentration, the same oil temperature of the temperature of salt water, the salt water of the oil mass 5%
It is 500 liters.
The beneficial effects of the invention are as follows:Combine purification Rice bran crude oil with sodium hydroxide using phosphoric acid, physically method of refining
So that technique simplifies, equipment investment is low, and environmentally friendly, refining effect is good;Twice using salt water cleaning, Rice bran crude oil has been ensured
Internal cleaning, purity is high.
Specific embodiment
In order to be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below it is right
The present invention is further described.
Embodiment:
A kind of refined rice bran oil combination degumming alkali refining method, specific step is as follows:
(1) oil stirring is thrown:By in 10 tons of Rice bran crude oil investment alkali refining tank, start uniform stirring;
(2) steam heats:Steam is opened to Rice bran crude oil and is heated to 70 DEG C;
(3) add phosphoric acid:Diluted phosphoric acid is added in Rice bran crude oil and is quickly stirred to react 15 minutes;
(4) adding sodium hydroxide:Sodium hydroxide needed for free fatty acid is totally removed is calculated according to the acid value of Rice bran crude oil
30% sodium hydroxide solution is added in amount;
(5) heating reaction:Rice bran oil is warming up to 80 DEG C, is reacted 5 minutes;
(6) add salt water:Salt water and the stirring of 500 liter of 10% concentration are added in rice bran oil, it is seen that after crystalline particle, immediately
Stop stirring;
(7) stratification:By rice bran oil stratification 6 hours or more, lower layer's soap stock is released;
(8) salt water secondary cleaning:Rice bran oil is washed two times with the salt water of oil mass 5%, soap stock is released, obtains edible vegetable oil.
The amount of sodium hydroxide in the step (3) needs to remove itself acid value, and the phosphoric acid is to have in 50 liters
30% concentration, the temperature of Rice bran crude oil is maintained at 70 DEG C when the described addition phosphoric acid.
Salt water in the step (6) is 10% concentration, the same oil temperature of the temperature of salt water, the salt water of the oil mass 5%
It is 500 liters.
Combine purification Rice bran crude oil with sodium hydroxide using phosphoric acid, physically method of refining simplifies technique, and equipment is thrown
Provide low, environmentally friendly, refining effect is good.
Twice using salt water cleaning, the cleaning inside Rice bran crude oil has been ensured, purity is high.
The grease phosphorus content of three other depickling methods, the comparative test of yield and color are resettled according to above-described embodiment,
As a result as follows:
Method of refining | Grease phosphorus content/ppm | Yield/% | Color |
First degumming chemical deacidification again | 150 | 65 | Kermesinus |
First degumming physical deacidification again | 180 | 71 | Peony |
Solvent method degumming depickling | 160 | 66 | Peony |
Combination degumming depickling | 100 | 72 | Light red |
As a result:Using the present invention relative to other traditional depickling methods, grease phosphorus content of the present invention is low, high income, and color is inclined
It is light, purity is high.
The basic principles, main features and advantages of the present invention have been shown and described above.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and what is described in the above embodiment and the description is only the present invention
Principle, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these variation and
Improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention is by appended claims and its equivalent
Object defines.
Claims (3)
1. a kind of refined rice bran oil combination degumming alkali refining method, it is characterised in that:Specific step is as follows for it:
(1) oil stirring is thrown:By in 10 tons of Rice bran crude oil investment alkali refining tank, start uniform stirring;
(2) steam heats:Steam is opened to Rice bran crude oil and is heated to 70 DEG C;
(3) add phosphoric acid:Diluted phosphoric acid is added in Rice bran crude oil and is quickly stirred to react 15 minutes;
(4) adding sodium hydroxide:The amount that sodium hydroxide needed for free fatty acid is totally removed is calculated according to the acid value of Rice bran crude oil, adds
Enter 30% sodium hydroxide solution;
(5) heating reaction:Rice bran oil is warming up to 80 DEG C, is reacted 5 minutes;
(6) add salt water:Salt water and the stirring of 500 liter of 10% concentration are added in rice bran oil, it is seen that after crystalline particle, stop immediately
Stirring;
(7) stratification:By rice bran oil stratification 6 hours or more, lower layer's soap stock is released;
(8) salt water secondary cleaning:Rice bran oil is washed two times with the salt water of oil mass 5%, soap stock is released, obtains edible vegetable oil.
2. a kind of refined rice bran oil according to claim 1 combination degumming alkali refining method, it is characterised in that:The step
(3) amount of the sodium hydroxide in needs to remove itself acid value, and the phosphoric acid is the concentration for having 30% in 50 liters, the addition
The temperature of Rice bran crude oil is maintained at 70 DEG C when phosphoric acid.
3. a kind of refined rice bran oil according to claim 1 combination degumming alkali refining method, it is characterised in that:The step
(6) salt water in is 10% concentration, and the same oil temperature of the temperature of salt water, the salt water of the oil mass 5% is 500 liters.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810671157.5A CN108841443A (en) | 2018-06-26 | 2018-06-26 | A kind of refined rice bran oil combination degumming alkali refining method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810671157.5A CN108841443A (en) | 2018-06-26 | 2018-06-26 | A kind of refined rice bran oil combination degumming alkali refining method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108841443A true CN108841443A (en) | 2018-11-20 |
Family
ID=64202342
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810671157.5A Pending CN108841443A (en) | 2018-06-26 | 2018-06-26 | A kind of refined rice bran oil combination degumming alkali refining method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108841443A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111378524A (en) * | 2018-12-29 | 2020-07-07 | 嘉里粮油(营口)有限公司 | Method for processing grease by using low-concentration phosphoric acid |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101238889A (en) * | 2008-03-14 | 2008-08-13 | 江南大学 | A method for refining rice bran oil by mixing crude rice bran oil refining process |
CN103614237A (en) * | 2013-12-12 | 2014-03-05 | 酉阳县康友粮油有限公司 | Rapeseed crude oil refining process |
CN105154220A (en) * | 2015-07-31 | 2015-12-16 | 崇州市白头甘泉工业油脂厂 | Degumming alkali-refining method for grease |
CN105713723A (en) * | 2016-03-31 | 2016-06-29 | 中粮(成都)粮油工业有限公司 | Crude oil refining method |
-
2018
- 2018-06-26 CN CN201810671157.5A patent/CN108841443A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101238889A (en) * | 2008-03-14 | 2008-08-13 | 江南大学 | A method for refining rice bran oil by mixing crude rice bran oil refining process |
CN103614237A (en) * | 2013-12-12 | 2014-03-05 | 酉阳县康友粮油有限公司 | Rapeseed crude oil refining process |
CN105154220A (en) * | 2015-07-31 | 2015-12-16 | 崇州市白头甘泉工业油脂厂 | Degumming alkali-refining method for grease |
CN105713723A (en) * | 2016-03-31 | 2016-06-29 | 中粮(成都)粮油工业有限公司 | Crude oil refining method |
Non-Patent Citations (2)
Title |
---|
彭阳生主编: "《植物油脂加工实用技术》", 31 March 2003, 金盾出版社 * |
柴本旺: "米糠油精炼工艺的研究", 《郑州粮食学院学报》 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111378524A (en) * | 2018-12-29 | 2020-07-07 | 嘉里粮油(营口)有限公司 | Method for processing grease by using low-concentration phosphoric acid |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101439593B (en) | Low-temperature processing technique for squeezing and refining pecan oil | |
CN102250683B (en) | Alkali refining process of cottonseed oil | |
CN101735886A (en) | Novel process for refining camellia seed crude oil | |
CN102934700B (en) | Refining method of rice oil | |
CN102533426A (en) | Processing method for improving flavor and nutritional quality of colza oil | |
CN104928023A (en) | Corn oil soap-free refining process | |
CN102234335A (en) | Production technology for continuously extracting starch, oil and sugar from cyperus esculentus | |
CN102816632A (en) | Method for digesting grease through microwave pretreatment and aqueous enzymatic method | |
CN101967423A (en) | Method for extracting tea oil by microwave-assisted aqueous enzymatic method | |
CN104629909B (en) | A kind of vegetable oil degumming method | |
CN102807916A (en) | Rice bran oil extraction method | |
CN106977582A (en) | A kind of method of Hydrolysis kinetics phytosterol in deodorization distillate | |
CN101172942A (en) | Method for producing calcium acetate with egg shell | |
CN104611132A (en) | Acid reducing process of rice oil | |
CN102041167B (en) | Method for preparing idesia polycarpa edible vegetable oil by immobilized enzyme and hot brine treatment process | |
CN101878820B (en) | Method for refining camellia oil with high nutrient content | |
CN108841443A (en) | A kind of refined rice bran oil combination degumming alkali refining method | |
CN104962388A (en) | Degumming process for edible vegetable oil | |
CN103074156A (en) | Method for employing double-bleaching technology in bleaching alkali-refined soybean oil | |
CN102826874B (en) | Method for producing potash magnesium sulphate fertilizers with unsaturation brine serving as flotation medium | |
CN103664532A (en) | Novel process for producing inositol | |
CN102732374A (en) | Production method for coldly squeezing corn and wheat compound embryo oil | |
CN103274432A (en) | Method for comprehensively utilizing hydrazine hydrate by-product sodium carbonate decahydrate through urea method | |
CN111518227B (en) | A kind of preparation method of agar glue | |
CN108165369A (en) | A kind of refining vegetable oil and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181120 |
|
RJ01 | Rejection of invention patent application after publication |