CN201451222U - Complete equipment for separating protein from rice bran - Google Patents
Complete equipment for separating protein from rice bran Download PDFInfo
- Publication number
- CN201451222U CN201451222U CN2009200895158U CN200920089515U CN201451222U CN 201451222 U CN201451222 U CN 201451222U CN 2009200895158 U CN2009200895158 U CN 2009200895158U CN 200920089515 U CN200920089515 U CN 200920089515U CN 201451222 U CN201451222 U CN 201451222U
- Authority
- CN
- China
- Prior art keywords
- discharging opening
- links
- charging aperture
- rice bran
- tube
- 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
Links
Images
Landscapes
- Cereal-Derived Products (AREA)
Abstract
The utility model relates to complete equipment for separating protein from rice bran, which can effectively solve the problems that the industrial extraction of protein from rice bran can meet the needs of food and beverage of people. The technical scheme is that a quantitative auger is sequentially connected with a bran and crushed rice separating sieve, a granulation machine and a fluidized bed through a hoisting machine, and the discharge port of the fluidized bed is connected with the feed port of an A canister desolventizing device; the discharge port of the A canister desolventizing device is connected with the feed port of a B canister desolventizing device, and the discharge port of the B canister desolventizing device is connected with an acid settling tank through a first extraction kettle and a first centrifuge which are connected in series; the discharge port of the acid settling tank is connected with the feed port of a centrifuge, and the discharge port of the centrifuge is connected with the feed port of a neutralizing tank; the discharge port of the neutralizing tank is connected with the feed port of a coarse strainer, and the discharge port of the coarse strainer is connected with the feed port of a flash tank; and the discharge port of the flash tank is connected with a spray drying tower. The utility model has simple, novel and unique structure, easy installation and use, low cost and good effect, can effectively solve the production problem of the industrial extraction of protein from rice bran, and has great economic and social benefits.
Description
One, technical field
The utility model relates to chemical field, particularly a kind of rice bran protein isolate complete set of equipments.
Two, background technology
Rice bran is a kind of inexpensive, nutritious rice processed side product, and China produces rice bran per year more than 1,400 ten thousand tons, is a kind of renewable resource that has a large capacity and a wide range.Rice bran contains the abundant nutrition material, and wherein protein content can be up to 18% in the defatted rice bran.At present, still as animal feed, therefore serious waste of resources, seeks new protein resource to most of rice bran from rice bran, increases the rice bran added value and has important practical significance.Rice bran protein is to generally acknowledge quality plant protein, its essential amino acid Compositional balance is reasonable, wherein lysine content is higher, for other vegetable protein incomparable, the rice bran protein biological value is very high, and its nutritive value can compare favourably with egg, cow's milk, and digestibility can reach more than 90%, and rice bran protein is a hypoallergenic albumen, is easy to people's food and drink and uses.Therefore, how effectively to utilize rice bran, extracting protein from rice bran is the technical barrier that need conscientiously solve, but for various reasons, not seeing so far has the report that extracts albumen equipment aspect from rice bran.
Three, utility model content
At above-mentioned situation; for overcoming the prior art defective; the purpose of the utility model just provides a kind of rice bran protein isolate complete set of equipments; can effectively solve industrialization extraction albumen from rice bran; to satisfy the problem of people's food and drink needs; the technical scheme of its solution is; quantitatively auger through elevator successively with the chaff bolter of dwelling; comminutor; fluid bed links to each other; the fluid bed discharging opening links to each other with A tube exsolution apparatus charging aperture; A tube exsolution apparatus discharging opening links to each other with B tube exsolution apparatus charging aperture; B tube exsolution apparatus discharging opening is through first extraction kettle of series connection; first centrifuge links to each other for heavy jar with acid; the heavy jar discharging opening of acid links to each other with the seperator charging aperture; the seperator discharging opening links to each other with the neutralizing tank charging aperture; the neutralizing tank discharging opening links to each other with the coarse filter charging aperture; the coarse filter discharging opening links to each other with the flash tank charging aperture; the flash tank discharging opening links to each other with spray drying tower; the utility model is simple in structure; novel unique; easily install and use; cost is low; effective, can effectively solve the production problem that albumen is extracted in from rice bran industrialization, economic and social benefit is huge.
Four, description of drawings
Accompanying drawing is a structure connection layout of the present utility model.
Five, the specific embodiment
Below in conjunction with accompanying drawing the specific embodiment of the present utility model is elaborated.
Shown in accompanying drawing; the utility model be quantitative auger 1 through elevator successively with the chaff bolter 3 of dwelling; comminutor 4; fluid bed 5 links to each other; fluid bed 5 discharging openings link to each other with A tube exsolution apparatus 10 charging apertures; A tube exsolution apparatus 10 discharging openings link to each other with B tube exsolution apparatus 13 charging apertures; B tube exsolution apparatus 13 discharging openings are through the first extraction kettle 14-1 of series connection; the first centrifuge 15-1 links to each other for heavy jar 17 with acid; heavy jar 17 discharging openings of acid link to each other with seperator 18 charging apertures; seperator 18 discharging openings link to each other with neutralizing tank 21 charging apertures; neutralizing tank 21 discharging openings link to each other with coarse filter 22 charging apertures; coarse filter 22 discharging openings link to each other with flash tank 24 charging apertures, and flash tank 24 discharging openings link to each other with spray drying tower 26.
In order to guarantee result of use, the discharging opening of said quantitative auger 1 and chaff are dwelt and between the charging aperture of bolter 3 the first elevator 2-1 are housed, chaff is dwelt and between the discharging opening of bolter 3 and comminutor 4 charging apertures second elevator 2-2 is housed, and between comminutor 4 discharging openings and fluid bed 5 charging apertures the 3rd elevator 2-3 is housed;
The first bent scraper plate 6-1 is housed between said fluid bed 5 discharging openings and buffer bin 7 charging apertures, and buffer bin 7 discharging openings link to each other with the charging aperture of infuser 9 through the second bent scraper plate 6-2, the first sealing auger 8-1 of series connection;
The discharging opening of said infuser 9 links to each other with A tube exsolution apparatus 10 charging apertures through the 3rd bent scraper plate 6-3, the second sealing auger 8-2 of series connection, is connected to condenser 12 through n-hexane blower fan 11 on the A tube exsolution apparatus 10;
Between said B tube exsolution apparatus 13 discharging openings and the first extraction kettle 14-1 discharging opening the 4th bent scraper plate 6-4 is housed;
The said first centrifuge 15-1 links to each other with heavy jar 17 charging apertures of acid through the first draw-off pump 16-1, the second extraction kettle 14-2, the second draw-off pump 16-2, the second centrifuge 15-2 of series connection;
Said seperator 18 adopts the horizontal spiral rod splitter, and its discharging opening links to each other through machine for decomposing and smashing 19, screw pump 20 and neutralizing tank 21 charging apertures of series connection;
Said coarse filter 22 discharging openings link to each other through the charging aperture of flash distillation sterilizer 23 with flash tank 24, and the discharging opening of flash tank 24 links to each other with spray drying tower 26 charging apertures through drawing pump 25.
Working condition of the present utility model is, comprise that the separation of (1) chaff crushed rices, (2) granulation, (3) oven dry, (4) leaching, (5) low temperature desolventizing, (6) degreasing dregs of rice single extraction, (7) first separation, (8) reextraction, (9) secondary separation, (10) acid are heavy, (11) separate curdled milk, (12) neutralization, (13) sterilization, (14) supercharging, spray-drying, (15) and pack and finish, specifically:
1, the chaff crushed rices separates: raw rice bran is delivered among the elevator 2-1 by quantitative auger 1, and elevator 2-1 is transported in the chaff crushed rices bolter 3 then, screens out foreign material such as the broken grain of rice that is mixed in the rice bran, clod, stone, for good basis is laid in back segment production;
2, granulation: the rice bran that comes out from chaff crushed rices bolter 3 is transported in the comminutor 4 with elevator 2-2, is processed into the chaff grain;
3, oven dry: the rice bran particle that comes out from comminutor 4 is delivered in the fluid bed 5 with elevator 2-3, and the rice bran particle is carried out drying, dehydration;
4, leach: be transported in the buffer bin 7 of leaching section by bent scraper plate 6-1 by the rice bran particle after drying, be transported among the sealing auger 8-1 with bent scraper plate 6-2, the rice bran particle is transported in the leaching lattice of infuser 9 by sealing auger 8-1, with the organic solvent-normal hexane circulated in countercurrent spray that circulates from top to bottom;
5, low temperature desolventizing: the rice bran particle that is come out by infuser enters among the bent scraper plate 6-3, the rice bran particle that comes out from bent scraper plate 6-3 is thus lifted among the sealing auger 8-2, enter then in the A tube exsolution apparatus 10, carry out precipitation one time, the rice bran particle seethes at A tube exsolution apparatus 10 medium speeds and advances, heated by the reverse hot solvent gas of crossing, solvent in the wet dregs of rice is evaporated with crossing the hot solvent gas, A tube exsolution apparatus 10 has the heating of interlayer cover, solvent gas in the A tube is taken away by n-hexane blower fan 11, enters condenser 12 and reclaims solvent;
Enter B tube exsolution apparatus 13 through the dregs of rice of A tube exsolution apparatus 10 through draught excluder and carry out the secondary precipitation, material in the B tube with the same in the A tube;
6, single extraction: the rice bran meal behind the low temperature desolventizing is sent into stirring in the single extraction still 14, reaction with bent scraper plate 6-4;
7, first separation: the mixed liquor of discharge separates chaff slag and protein emulsion through centrifuge 15-1;
8, reextraction: residual protein in the chaff slag that single extraction is separated, be transported in the extraction kettle through pump 16-1, add warm water and NaOH solution once more and adjust solution to pH value;
9, secondary separation: extraction fluid is transported to by pump 16-2 separates bran slag and protein liquid among the centrifuge 15-2;
10, acid is heavy: once pump in heavy jar 17 of the acid with the emulsion that obtains after the secondary collection is separated and stir, add defoamer and warm water and sodium sulfite, the survey pH value;
11, separate curdled milk: separate clear liquid and curdled milk, effluent discharge with horizontal screw seperator 18;
12, neutralization: separate after broken curdled milk be transported in the neutralizing tank 21 with screw pump 20, add the neutralization of NaOH solution, the logical cold water of neutralizing tank chuck cools off;
13, sterilization: the emulsion after the neutralization is slightly considered through coarse filter 22 earlier, in case the pimple plug nozzle in the curdled milk enters 23 sterilizations of flash distillation sterilizer then, enter flash tank 24 very easily colloidizations of chilled feed liquid, to be detained in order not making in jar, drawing pump 25 often to be in Light Condition;
14, supercharging, spray-drying:, the emulsion of coming out from drawing pump 25 is transported to the spray drying tower 26, dehydrates processing, and as protein product moisture height, the air themperature height will increase air quantity, prevents out damp powder and caking;
15, packing: the protein isolate goods sieve or directly bore end blowing down from spray tower, go into bag, seal, and packing will be carried out under ultraviolet ray.
Positive contribution of the present utility model is: will have known each parts now and extract the suitability for industrialized production needs of protein isolate through scientific and reasonable combination from rice bran, be combined into complete being used to and extract the complete set of equipments of albumen, and through using, obtained satisfied effect, solved the need of industrial production of from rice bran, extracting albumen effectively, the product of the utility model production meets the edible protein quality index after tested fully, specifically:
Structural state: loose powdery, do not lump,
Color and luster: have the intrinsic milky of powdery rice bran protein, uniformity
Smell: have the intrinsic smell of powdery rice bran protein, free from extraneous odour
Crude protein: 〉=85%
Moisture :≤7%
NSI：≥80％
Crude fat :≤1%
Ash content :≤3.8%
PH value: 6.8-7.2
Arsenic (mg/kg is in As) :≤0.5%
Aluminium (mg/kg is in Pn) :≤1.0%
Total number of bacteria :≤3000,
From the above, the utility model adopts the equipment of science to connect and compose and extract protein isolate from rice bran, has solved industrialization effectively from rice bran protein isolate technology technical barrier, has increased the added value of rice bran meal, and economic and social benefit is huge.
Claims (8)
1. rice bran protein isolate complete set of equipments; it is characterized in that; quantitatively auger (1) through elevator successively with the chaff bolter (3) of dwelling; comminutor (4); fluid bed (5) links to each other; fluid bed (5) discharging opening links to each other with A tube exsolution apparatus (10) charging aperture; A tube exsolution apparatus (10) discharging opening links to each other with B tube exsolution apparatus (13) charging aperture; B tube exsolution apparatus (13) discharging opening is through first extraction kettle (14-1) of series connection; first centrifuge (15-1) links to each other with acid heavy jar (17); the heavy jar of same seperator of (17) discharging opening (18) charging aperture of acid links to each other; the same neutralizing tank of seperator (18) discharging opening (21) charging aperture links to each other; the same coarse filter of neutralizing tank (21) discharging opening (22) charging aperture links to each other; the same flash tank of coarse filter (22) discharging opening (24) charging aperture links to each other, and the same spray drying tower of flash tank (24) discharging opening (26) links to each other.
2. rice bran protein isolate complete set of equipments according to claim 1; it is characterized in that; the discharging opening of said quantitative auger (1) and chaff are dwelt and between the charging aperture of bolter (3) first elevator (2-1) are housed; chaff is dwelt and between the discharging opening of bolter (3) and comminutor (4) charging aperture second elevator (2-2) is housed, and between comminutor (4) discharging opening and fluid bed (5) charging aperture the 3rd elevator (2-3) is housed.
3. rice bran protein isolate complete set of equipments according to claim 1, it is characterized in that, between said fluid bed (5) discharging opening and buffer bin (7) charging aperture the first bent scraper plate (6-1) is housed, buffer bin (7) discharging opening links to each other through the second bent scraper plate (6-2) of series connection, the charging aperture of the first sealing same infuser of auger (8-1) (9).
4. rice bran protein isolate complete set of equipments according to claim 1, it is characterized in that, the discharging opening of said infuser (9) links to each other with A tube exsolution apparatus (10) charging aperture through the 3rd bent scraper plate (6-3), the second sealing auger (8-2) of series connection, and A tube exsolution apparatus (10) is gone up and is connected to condenser (12) through n-hexane blower fan (11).
5. rice bran protein isolate complete set of equipments according to claim 1 is characterized in that, between said B tube exsolution apparatus (13) discharging opening and first extraction kettle (14-1) discharging opening the 4th bent scraper plate (6-4) is housed.
6. rice bran protein isolate complete set of equipments according to claim 1, it is characterized in that said first centrifuge (15-1) links to each other with heavy jar (17) charging aperture of acid through first draw-off pump (16-1), second extraction kettle (14-2), second draw-off pump (16-2), second centrifuge (15-2) of series connection.
7. rice bran protein isolate complete set of equipments according to claim 1 is characterized in that, said seperator (18) adopts the horizontal spiral rod splitter, and its discharging opening links to each other through machine for decomposing and smashing (19), screw pump (20) and neutralizing tank (21) charging aperture of series connection.
8. rice bran protein isolate complete set of equipments according to claim 1, it is characterized in that, said coarse filter (22) discharging opening links to each other through the charging aperture of flash distillation sterilizer (23) with flash tank (24), and the discharging opening of flash tank (24) links to each other through the same spray drying tower of drawing pump (25) (26) charging aperture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200895158U CN201451222U (en) | 2009-04-10 | 2009-04-10 | Complete equipment for separating protein from rice bran |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200895158U CN201451222U (en) | 2009-04-10 | 2009-04-10 | Complete equipment for separating protein from rice bran |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201451222U true CN201451222U (en) | 2010-05-12 |
Family
ID=42378550
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200895158U Expired - Fee Related CN201451222U (en) | 2009-04-10 | 2009-04-10 | Complete equipment for separating protein from rice bran |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201451222U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107853449A (en) * | 2017-11-07 | 2018-03-30 | 山东禹王生态食业有限公司 | A kind of heavy tank of soybean protein acid and the heavy method of soybean protein processing acid |
| CN108378192A (en) * | 2018-03-21 | 2018-08-10 | 山东禹王生态食业有限公司 | A kind of broken system and method for soybean protein isolate solution |
-
2009
- 2009-04-10 CN CN2009200895158U patent/CN201451222U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107853449A (en) * | 2017-11-07 | 2018-03-30 | 山东禹王生态食业有限公司 | A kind of heavy tank of soybean protein acid and the heavy method of soybean protein processing acid |
| CN108378192A (en) * | 2018-03-21 | 2018-08-10 | 山东禹王生态食业有限公司 | A kind of broken system and method for soybean protein isolate solution |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101536727B (en) | Production method for extracting and separating protein from rice bran | |
| AU2002304796B9 (en) | Method and system for preparing extraction meal from sun flower seeds for animal feed | |
| CN101439593B (en) | Low-temperature processing technique for squeezing and refining pecan oil | |
| CN104450168B (en) | A kind of method of cold pressing and Physical refining camellia seed oil | |
| CN101177647B (en) | Laportea urentissima grease processing technology | |
| CN101268803A (en) | Processing method for castoff of food and drink | |
| CN101176504A (en) | Technique of processing Huoma albumen powder | |
| CN106010719B (en) | A kind of method and device manufacturing biomass fuel with urban waste | |
| CN108741078A (en) | The processing method for preparing the method and linseed of flaxseed gum, flax lignan, flax dietary fiber and flax protein powder | |
| CN106903131A (en) | A kind of kitchen garbage fermentation system, method and fermented feed | |
| CN101138386B (en) | Method for producing feedstuff coarse albumen powder by kitchen waste | |
| CN109793099A (en) | A kind for the treatment of process of Xinhui citrus reticulata pulp | |
| CN104232295A (en) | Corn germ grease supercritical extraction system and method | |
| CN201451222U (en) | Complete equipment for separating protein from rice bran | |
| WO2014084718A1 (en) | A process for extracting residual oil from oil bearing waste feedstock | |
| CN101779775B (en) | Tomato skin, seed and residue dehydration drying and dry method skin and seed separation and combination production method in tomato paste factory | |
| CN107594547A (en) | A kind of device that soybean fiber powder is produced using the wet bean dregs of soybean protein isolate as raw material | |
| CN106590915A (en) | Processing method of camellia oil | |
| CN100563462C (en) | The beans comprehensive utilization process | |
| CN106632586B (en) | Method for simultaneously extracting starch and protein | |
| CN101579684A (en) | Urban catering pigwash industrialized treatment method | |
| CN101019603B (en) | Process of producing active protein and oil with maggot and earth worm | |
| CN102450384A (en) | Method for extracting soybean protein from soybean oil residues | |
| CN205074325U (en) | Wet processing apparatus that separates of kitchen garbage | |
| CN208667645U (en) | The extraction element of Residual oil in a kind of cold press rap oil seedcake |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100512 Termination date: 20150410 |
|
| EXPY | Termination of patent right or utility model |