CN109749842A - A kind of animal oil extraction process low in calories - Google Patents
A kind of animal oil extraction process low in calories Download PDFInfo
- Publication number
- CN109749842A CN109749842A CN201910124823.8A CN201910124823A CN109749842A CN 109749842 A CN109749842 A CN 109749842A CN 201910124823 A CN201910124823 A CN 201910124823A CN 109749842 A CN109749842 A CN 109749842A
- Authority
- CN
- China
- Prior art keywords
- animal
- calories
- tallow
- oil
- conduction liquid
- 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
Landscapes
- Fats And Perfumes (AREA)
Abstract
The invention discloses a kind of animal oil extraction processes low in calories, comprising the following steps: S1: cleaning and crush, and cleans to fresh animal tallow, is crushed by crusher to animal tallow after cleaning, and smashed animal tallow is in " jujube shape ";S2: the pre-heat treatment will be added in process tank by S1 treated animal tallow, heat to animal tallow, and heating temperature is 30 degree, heating 30 minutes;S3: electrolysis is fuel-displaced, and in by S2 treated animal tallow, conduction liquid is added, is powered to conduction liquid, current strength 50A, so that oil liquid is constantly precipitated;S4: filter centrifugation separation, to by S3, treated that mixture is filtered.The invention proposes a kind of animal oil extraction processes low in calories, and using the method for the electrolysis that is powered, so that the animal oil in animal fat is quickly precipitated, simple process, preparation speed is fast, and preparation temperature is low, and grease impurities produced are few, and oil colours is good, and condition is high.
Description
Technical field
The present invention relates to Oil processing technical fields, more particularly to a kind of animal oil extraction process low in calories.
Background technique
Animal oil, i.e. animal fat, are the fat of animal, are typically derived from pig, ox, fish for the animal oil that the mankind eat
Deng, can be used for processed food, enable food have meat fresh perfume (or spice).Oil biggish vegetarian diet, such as eggplant, radish etc., meeting are eaten in collocation
Have and make us the effect of appetite is opened greatly, promotes absorption of the human body to food materials nutrition especially vitamin.Animal oil taste is more fragrant, has
Promote the absorption of fat-soluble A, D, E, K etc..In addition, the weight of cholesterol or human tissue cell in animal oil
Ingredient is wanted, is the important source material for synthesizing bile and certain hormones.
The extracting method of animal oil has at present: squeezing method, cooking process, light alkali hydrolysis method, solvent method, enzymatic isolation method and overcritical
Fluids extraction etc..
What wherein application was wider is cooking process and light alkali hydrolysis method.Cooking process cannot separate the fat in conjunction with protein
It comes, therefore recovery rate is relatively low, and the temperature extracted affects the quality for extracting fat generally all at 90 °C or so.
Other nutritional ingredients further cannot be utilized efficiently after light alkali hydrolysis method mentions oil, cause very big waste.
Rule is squeezed firstly the need of high temperature drying, thus the animal oil produced is second-rate that (active lipid ingredient is impaired tight
Weight), and recovery rate is lower.Solvent method need to expend a large amount of organic solvent, and solvent easily remains in product.
Enzymatic isolation method is the hydrolysis using protease to protein, keeps the grease in conjunction with protein sufficiently free, but
The higher cost of enzyme.
Supercritical fluid extraction experiment scale of input is larger, fund is more, is relatively suitably applied the crude fish oil processing later period
The separating-purifying of physiological activator EPA and DHA, thus it is proposed that a kind of animal oil extraction process low in calories.
Summary of the invention
The purpose of the present invention is to solve disadvantages existing in the prior art, and the animal oil that the one kind proposed is low in calories
Extraction process.
A kind of animal oil extraction process low in calories, comprising the following steps:
S1: cleaning and crush, and cleans to fresh animal tallow, is crushed by crusher to animal tallow after cleaning,
Smashed animal tallow is in " jujube shape ";
S2: the pre-heat treatment will be added in process tank by S1 treated animal tallow, heat to animal tallow, heat
Temperature is 30-50 degree, is heated 30 to 50 minutes;
S3: electrolysis is fuel-displaced, and in by S2 treated animal tallow, conduction liquid is added, is powered to conduction liquid, current strength is
50-100A so that oil liquid is constantly precipitated;
S4: filter centrifugation separation, to by S3, treated that mixture is filtered, then to the animal oil of conduction liquid and precipitation
It is centrifuged, isolates animal oil therein.
Preferably, the conduction liquid is salt water, and brine strength is the sodium chloride solution of 2%-8%.
Preferably, it in the S3 step, when carrying out being electrolysed fuel-displaced, is constantly stirred, so that conduction liquid and tallow
Fat comes into full contact with.
Preferably, it in the S4 step, first passes through filter screen and the mixed liquor after S3 electrolysis is filtered, then pass through again
Conduction liquid and the animal oil of precipitation is centrifuged in centrifugal device.
Preferably, it after cleaning and crush animal fat in the S1 step, needs to take off smashed animal fat
Water.
Preferably, it when carrying out being electrolysed fuel-displaced to grease in the S3 step, is taken off when animal fat diameter is less than 1 centimetre
Oil finishes.
The invention proposes a kind of animal oil extraction processes low in calories, using the method for the electrolysis that is powered, so that animal oil
Animal oil in rouge is quickly precipitated, simple process, and preparation speed is fast, and preparation temperature is low, and grease impurities produced are few, oil colours
Good, condition is high.
Specific embodiment
Combined with specific embodiments below the present invention is made further to explain.
Embodiment one
One kind proposed by the present invention animal oil extraction process low in calories, comprising the following steps:
S1: cleaning and crush, and cleans to fresh animal tallow, is crushed by crusher to animal tallow after cleaning,
Smashed animal tallow is in " jujube shape ";
S2: the pre-heat treatment will be added in process tank by S1 treated animal tallow, heat to animal tallow, heat
Temperature is 30 degree, is heated 30 minutes;
S3: electrolysis is fuel-displaced, and in by S2 treated animal tallow, conduction liquid is added, is powered to conduction liquid, current strength is
50A so that oil liquid is constantly precipitated;
S4: filter centrifugation separation, to by S3, treated that mixture is filtered, then to the animal oil of conduction liquid and precipitation
It is centrifuged, isolates animal oil therein.
The conduction liquid is salt water, and the sodium chloride solution that brine strength is 2% is fuel-displaced be electrolysed in the S3 step
When, it is constantly stirred, so that conduction liquid comes into full contact with animal tallow, in the S4 step, first passes through filter screen to S3 electricity
Mixed liquor after solution is filtered, and then conduction liquid and the animal oil of precipitation is centrifuged by centrifugal device again, institute
It states after being cleaned and crush in S1 step to animal fat, needs to be dehydrated smashed animal fat, it is right in the S3 step
When grease carries out being electrolysed fuel-displaced, de-oiling is finished when animal fat diameter is less than 1 centimetre.
Embodiment two
One kind proposed by the present invention animal oil extraction process low in calories, comprising the following steps:
S1: cleaning and crush, and cleans to fresh animal tallow, is crushed by crusher to animal tallow after cleaning,
Smashed animal tallow is in " jujube shape ";
S2: the pre-heat treatment will be added in process tank by S1 treated animal tallow, heat to animal tallow, heat
Temperature is 40 degree, is heated 40 minutes;
S3: electrolysis is fuel-displaced, and in by S2 treated animal tallow, conduction liquid is added, is powered to conduction liquid, current strength is
75A so that oil liquid is constantly precipitated;
S4: filter centrifugation separation, to by S3, treated that mixture is filtered, then to the animal oil of conduction liquid and precipitation
It is centrifuged, isolates animal oil therein.
The conduction liquid is salt water, and the sodium chloride solution that brine strength is 5% is fuel-displaced be electrolysed in the S3 step
When, it is constantly stirred, so that conduction liquid comes into full contact with animal tallow, in the S4 step, first passes through filter screen to S3 electricity
Mixed liquor after solution is filtered, and then conduction liquid and the animal oil of precipitation is centrifuged by centrifugal device again, institute
It states after being cleaned and crush in S1 step to animal fat, needs to be dehydrated smashed animal fat, it is right in the S3 step
When grease carries out being electrolysed fuel-displaced, de-oiling is finished when animal fat diameter is less than 1 centimetre.
Embodiment three
One kind proposed by the present invention animal oil extraction process low in calories, comprising the following steps:
S1: cleaning and crush, and cleans to fresh animal tallow, is crushed by crusher to animal tallow after cleaning,
Smashed animal tallow is in " jujube shape ";
S2: the pre-heat treatment will be added in process tank by S1 treated animal tallow, heat to animal tallow, heat
Temperature is 50 degree, is heated 50 minutes;
S3: electrolysis is fuel-displaced, and in by S2 treated animal tallow, conduction liquid is added, is powered to conduction liquid, current strength is
100A so that oil liquid is constantly precipitated;
S4: filter centrifugation separation, to by S3, treated that mixture is filtered, then to the animal oil of conduction liquid and precipitation
It is centrifuged, isolates animal oil therein.
The conduction liquid is salt water, and the sodium chloride solution that brine strength is 8% is fuel-displaced be electrolysed in the S3 step
When, it is constantly stirred, so that conduction liquid comes into full contact with animal tallow, in the S4 step, first passes through filter screen to S3 electricity
Mixed liquor after solution is filtered, and then conduction liquid and the animal oil of precipitation is centrifuged by centrifugal device again, institute
It states after being cleaned and crush in S1 step to animal fat, needs to be dehydrated smashed animal fat, it is right in the S3 step
When grease carries out being electrolysed fuel-displaced, de-oiling is finished when animal fat diameter is less than 1 centimetre.
3 animal oil of above three embodiments embodiment is produced fastest, and oil quality is slightly worse, 1 animal oil oil system of embodiment
Take speed most slow, oil quality is best, and the quality and speed for the oil that embodiment 2 is produced are all more outstanding, chooses the implementation of embodiment 2
Mode is best.
The foregoing is only a preferred embodiment of the present invention, but scope of protection of the present invention is not limited thereto,
Anyone skilled in the art in the technical scope disclosed by the present invention, according to the technique and scheme of the present invention and its
Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.
Claims (6)
1. a kind of animal oil extraction process low in calories, which comprises the following steps:
S1: cleaning and crush, and cleans to fresh animal tallow, is crushed by crusher to animal tallow after cleaning,
Smashed animal tallow is in " jujube shape ";
S2: the pre-heat treatment will be added in process tank by S1 treated animal tallow, heat to animal tallow, heat
Temperature is 30-50 degree, is heated 30 to 50 minutes;
S3: electrolysis is fuel-displaced, and in by S2 treated animal tallow, conduction liquid is added, is powered to conduction liquid, current strength is
50-100A so that oil liquid is constantly precipitated;
S4: filter centrifugation separation, to by S3, treated that mixture is filtered, then to the animal oil of conduction liquid and precipitation
It is centrifuged, isolates animal oil therein.
2. one kind according to claim 1 animal oil extraction process low in calories, which is characterized in that the conduction liquid is salt
Water, brine strength are the sodium chloride solution of 2%-8%.
3. one kind according to claim 1 animal oil extraction process low in calories, which is characterized in that in the S3 step,
It when carrying out being electrolysed fuel-displaced, is constantly stirred, so that conduction liquid comes into full contact with animal tallow.
4. one kind according to claim 1 animal oil extraction process low in calories, which is characterized in that in the S4 step,
It first passes through filter screen to be filtered the mixed liquor after S3 electrolysis, then again by centrifugal device to the animal of conduction liquid and precipitation
Oil is centrifuged.
5. one kind according to claim 1 animal oil extraction process low in calories, which is characterized in that right in the S1 step
After animal fat cleans and crush, need to be dehydrated smashed animal fat.
6. one kind according to claim 1 animal oil extraction process low in calories, which is characterized in that right in the S3 step
When grease carries out being electrolysed fuel-displaced, de-oiling is finished when animal fat diameter is less than 1 centimetre.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910124823.8A CN109749842A (en) | 2019-02-20 | 2019-02-20 | A kind of animal oil extraction process low in calories |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910124823.8A CN109749842A (en) | 2019-02-20 | 2019-02-20 | A kind of animal oil extraction process low in calories |
Publications (1)
Publication Number | Publication Date |
---|---|
CN109749842A true CN109749842A (en) | 2019-05-14 |
Family
ID=66406553
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910124823.8A Pending CN109749842A (en) | 2019-02-20 | 2019-02-20 | A kind of animal oil extraction process low in calories |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109749842A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB520285A (en) * | 1937-10-14 | 1940-04-19 | Separator Ab | A process for the refining of vegetable and animal oils or fats |
CN108285826A (en) * | 2018-01-30 | 2018-07-17 | 中国海洋大学 | A kind of animal oil extracting method |
CN108559621A (en) * | 2018-06-26 | 2018-09-21 | 新乡市红阳油脂工程技术有限公司 | A kind of animal fat Environment-friendlyextraction extraction method |
-
2019
- 2019-02-20 CN CN201910124823.8A patent/CN109749842A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB520285A (en) * | 1937-10-14 | 1940-04-19 | Separator Ab | A process for the refining of vegetable and animal oils or fats |
CN108285826A (en) * | 2018-01-30 | 2018-07-17 | 中国海洋大学 | A kind of animal oil extracting method |
CN108559621A (en) * | 2018-06-26 | 2018-09-21 | 新乡市红阳油脂工程技术有限公司 | A kind of animal fat Environment-friendlyextraction extraction method |
Non-Patent Citations (1)
Title |
---|
张庆荣等主编: "《高等学校试用教材 工程机械修理学 上册》", 31 July 1979, 人民交通出版社 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US10455849B2 (en) | Method for the preparation of a protein peptide, a protein peptide and use thereof | |
JP6483252B2 (en) | Fish protein oligopeptide with low allergenicity and reduced fish odor, industrial preparation method thereof, and use thereof | |
JP6308950B2 (en) | Process for treating crustaceans to produce their low fluoride / low trimethylamine products | |
CN103843970B (en) | Production method for preparing ossein oligopeptide meal, bone oil and bone meal | |
JP2007068454A (en) | Method for producing rice protein, rice protein produced by the method, and food | |
US11129400B2 (en) | Method of ecological utilization of silver carp | |
EP2332424A1 (en) | Method for producing lipid | |
CN104432111A (en) | Rice bran soluble dietary fiber, production technology and application thereof | |
EP3516966A1 (en) | A concentrated krill protein hydrolysate fraction | |
CN101812111A (en) | Comprehensive deep processing method for oil tea fruits | |
CN105779098A (en) | Method for refining fish oil from leftovers of freshwater fish | |
CN107142294A (en) | The method that collagen peptides products are prepared by raw material of deerskin | |
CN105341933A (en) | Trepang and oyster enzymolysis oral liquid and preparation method thereof | |
CN101397581A (en) | Method for extracting fishskin collagen polypeptide from fish wastes | |
CN106387304A (en) | Method for preparing abalone viscera phospholipid through HPEF (High Pulsed Electric Field)-coupled biological enzymolysis | |
CN105316382A (en) | Preparation method of fishbone collagen | |
CN100579377C (en) | Method for extracting coconut oil from coconut bran | |
CN106804873A (en) | A kind of preparation technology of gel soybean protein isolate high | |
Laplante et al. | Comparison of low‐temperature processes for oil and coenzyme Q10 extraction from mackerel and herring | |
CN109749842A (en) | A kind of animal oil extraction process low in calories | |
KR20160030603A (en) | Using proteolytic enzyme extracted marsh clam extract, and manufacturing method thereof | |
CN111296755A (en) | A nutrition-enriched oatmeal food containing marine chondroitin sulfate and its preparation method | |
COBB III et al. | Development of a process for preparing a fish protein concentrate with rehydration and emulsifying capacities | |
CN109221597A (en) | A kind of preparation method of river Puffer fish low fat albumen powder | |
US1851253A (en) | Treating albuminoid substances |
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 | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20190514 |
|
WD01 | Invention patent application deemed withdrawn after publication |