CN201433185Y - Complete sets of equipment for cottonseed pretreatment and extraction production of dephenolization cottonseed protein - Google Patents
Complete sets of equipment for cottonseed pretreatment and extraction production of dephenolization cottonseed protein Download PDFInfo
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- CN201433185Y CN201433185Y CN2009200912914U CN200920091291U CN201433185Y CN 201433185 Y CN201433185 Y CN 201433185Y CN 2009200912914 U CN2009200912914 U CN 2009200912914U CN 200920091291 U CN200920091291 U CN 200920091291U CN 201433185 Y CN201433185 Y CN 201433185Y
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Abstract
The utility model relates to complete sets of equipment for cottonseed pretreatment and extraction production of dephenolization cottonseed protein, which can effectively solve the problem of dephenolization protein production by making full use of cottonseed cakes after cottonseed oil pressing. The complete sets of equipment adopts the structure that a scrapper conveyer is connected with an inletof a towline type leacher through an enclosed auger; the scrapper conveyer, a mixed oil filter and a solvent pump are respectively connected on the towline type leacher, the scrapper conveyer is connected with a dryer through the enclosed auger, and the scraper conveyer and a trap are connected on the dryer, and are connected with a conditioner; the scraper conveyer is connected with a dephenolization protein finished product warehouse through a flat scraper conveyer; the trap is connected with a methanol liquid dispensing tank through a condenser, and is connected with a flash evaporizationbox, the condenser and a layer-disc stripper through a mixed oil tank and an evaporator; the layer-disc stripper is connected with the condenser and a crude oil tank which is connected with a cottonseed oil house through an oil pump. The equipment has the advantages of novel and unique structure, good using effect and high production efficiency, and can simultaneously solve the problem of industrialized production of dephenolization protein and cottonseed oil, thereby having great economical and social benefits.
Description
One, technical field
The utility model relates to chemical machinery, and cotton seed dephenolizing protein complete equipment is produced in a kind of cottonseed pre-treatment, the extraction that particularly utilize cottonseed to extract Oleum Gossypii semen and extraction production cotton seed dephenolizing protein suitability for industrialized production.
Two, background technology
China is the main in the world cotton big country that produces, and produces about 1,100 ten thousand tons of cottonseed per year, and cottonseed is not only good oil resource, also is a kind of urgency major protein resource to be developed.
It is about 50～55% to contain cotton benevolence in the cottonseed, and oil-containing 30～35% in the cotton benevolence, contain albumen 35～38%.Cottonseed cake after the oil expression (dregs of rice) contains a large amount of albumen, because general cottonseed contains a kind of toxin " gossypol ", therefore, also field of fertilizer is assigned cotton cake dregs as in many places, and the addition of cottonseed cake (dregs of rice) in feed is very little, is generally 3-4%.Yet China's protein fodder wretched insufficiency, mixing (joining), to close the feedstuff protein level low, restricting the development that livestock industry is produced.By 2008, China's feed consumption surpassed 100,000,000 tons, and the breach of protein raw materials is more than 1,000 ten thousand tons.If cottonseed is fully used, the whole nation can get 3,900,000 tons high-quality cottonseed feedstuff protein every year.Develop high-quality cottonseed feedstuff protein, promise well for Chinese market.
Because cottonseed is a kind of good oil resource, the present situation of cottonseed processing industry, it mainly is 2. to press in advance by 1. screw press to leach 3. directly stripping (once leaching) and wait and produce grease that traditional cottonseed processing industry is produced, the Oleum Gossypii semen that extracts is the legacy equipment main products, and traditional cottonseed processing industry product structure is: 1. 2. 3. 4. oil foot (soap stock) (pressing sorting out value) of cotton seed hulls of cottonseed cake (cotton dregs) of Oleum Gossypii semen.Contain a large amount of gossypols (or in conjunction with gossypol) toxicity in oil expression or the pre-cottonseed cake (cotton dregs) that obtains after the leaching that presses, squeeze by high temperature simultaneously, make protein denaturation, so cottonseed cake (cotton dregs) can only be as the after-product of cottonseed processing industry, use in feed, food service industry is restricted, except ruminating animal that a spot of degreasing grouts are used to feed, have to its as fertilizer sources in a lot of areas, lost its original value, this is a kind of waste of protein resource under present human situation as feeding or table egg daytime sense shortage.Therefore, how effectively to utilize cottonseed to solve proteic production problem, be that people wish the technical problem that solves always.
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 cottonseed pre-treatment, cotton seed dephenolizing protein complete equipment is produced in extraction, can effectively solve the problem that the cottonseed cake (cotton dregs) after cottonseed extracts oil is produced dephenolizing protein that makes full use of, the technical scheme of its solution is, include the feeding pot of serial connection successively, first lift, first stirs cage, seed cleaner, the discaling roll Cottonseed shucking machine, angle sieve, wind riddle, second lift, horizontal softening kettle, first scraper conveyor, the first flat scraper conveyor, the pair roller flaker, second scraper conveyor, the second flat scraper conveyor, plate dryer, the 3rd scraper conveyor, the 3rd flat scraper conveyor, feed box and the 4th scraper conveyor, the 4th scraper conveyor stirs cage through first sealing and links to each other with the import of drag chain leacher, be connected to the 5th scraper conveyor respectively in three outlets of drag chain leacher, hybrid oil filter machine and solvent pump, it is continuous with the import of first drying machine that the 5th scraper conveyor stirs cage through second sealing, be connected to the 6th scraper conveyor respectively in two outlets of first drying machine, first trap, it is continuous with the import of second drying machine that the 6th scraper conveyor stirs cage through the 3rd sealing, two outlets of second drying machine are respectively with the 7th scraper conveyor, the import of second trap links to each other, the outlet of the 7th scraper conveyor is stirred cage through the 4th sealing and is linked to each other with the import of quality-adjusting device, two outlets of quality-adjusting device link to each other with the import of the 8th scraper conveyor and the 3rd trap respectively, the outlet of the 8th scraper conveyor links to each other with the dephenolizing protein stockyard through Siping City's scraper conveyor, second trap links to each other with the second methyl alcohol separating box through second condenser, the second methyl alcohol separating box is through miscella tank, first long-tube evaportor links to each other with the import of the first shwoot case, be connected to the 5th condenser respectively in two outlets of the first shwoot case, second long-tube evaportor, second long-tube evaportor links to each other with the import of the second shwoot case, two outlets of the second shwoot case are respectively with the 6th condenser, layer dish stripping tower links to each other, two outlets of layer dish stripping tower are respectively with the 7th condenser, the crude oil jar links to each other, the crude oil jar through oil pump with cotton oil storehouse link to each other (entering the refining plant), the utility model novel structure uniqueness, result of use is good, the production efficiency height, can solve the problem of suitability for industrialized production dephenolizing protein and Oleum Gossypii semen simultaneously, economic and social benefit is huge.
Four, description of drawings
Accompanying drawing is a device structure interface chart of the present utility model.
Five, embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is elaborated.
Shown in accompanying drawing, the utility model includes the feeding pot 1 of serial connection successively, the first lift 2-1, first stirs cage 3-1, seed cleaner 4, discaling roll Cottonseed shucking machine 5, angle sieve 6, wind riddle 7, the second lift 2-2, horizontal softening kettle 8, the first scraper conveyor 9-1, the first flat scraper conveyor 10-1, pair roller flaker 11, the second scraper conveyor 9-2, the second flat scraper conveyor 10-2, plate dryer 12, the 3rd scraper conveyor 9-3, the 3rd flat scraper conveyor 10-3, feed box 13 and the 4th scraper conveyor 9-4, the 4th scraper conveyor 9-4 stirs cage 14-1 through first sealing and links to each other with 15 imports of drag chain leacher, be connected to the 5th scraper conveyor 9-5 respectively in three outlets of drag chain leacher 15, hybrid oil filter machine 26 and solvent pump 25, it is continuous with the import of the first drying machine 16-1 that the 5th scraper conveyor 9-5 stirs cage 14-2 through second sealing, be connected to the 6th scraper conveyor 9-6 respectively in two outlets of the first drying machine 16-1, the first trap 18-1, it is continuous with the import of the second drying machine 16-2 that the 6th scraper conveyor 9-6 stirs cage 14-3 through the 3rd sealing, two outlets of the second drying machine 16-2 are respectively with the 7th scraper conveyor 9-7, the import of the second trap 18-2 links to each other, the 7th scraper conveyor 9-7 outlet is stirred cage 14-4 through the 4th sealing and is linked to each other with the import of quality-adjusting device 17, two outlets of quality-adjusting device 17 link to each other with the import of the 8th scraper conveyor 9-8 and the 3rd trap 18-3 respectively, the outlet of the 8th scraper conveyor 9-8 links to each other with the dephenolizing protein stockyard through the scraper conveyor 10-4 of Siping City, the second trap 18-2 links to each other with the second methyl alcohol separating box 20-2 through the second condenser 19-2, the second methyl alcohol separating box 20-2 is through miscella tank 24, the first long-tube evaportor 27-1 links to each other with the import of the first shwoot case 28-1, be connected to the 5th condenser 19-5 respectively in two outlets of the first shwoot case 28-1, the second long-tube evaportor 27-2, the second long-tube evaportor 27-2 links to each other with the import of the second shwoot case 28-2, two outlets of the second shwoot case 28-2 are respectively with the 6th condenser 19-6, layer dish stripping tower 29 links to each other, two outlets of layer dish stripping tower 29 are respectively with the 7th condenser 19-7, crude oil jar 30 links to each other, crude oil jar 30 through oil pump 31 with cotton oil storehouse link to each other (entering the refining plant).
In order to guarantee the comprehensive utilization ratio of result of use and raising raw material, the second strand cage 3-2 is housed on the pipeline between said angle sieve 6, the wind riddle 7, be provided with the 3rd between wind riddle 7, the 4th strand cage 3-4 and stir cage 3-3; Said first trap 18-1 outlet links to each other with the import of the first methyl alcohol separating box 20-1 through the first condenser 19-1, methanol tank 21 and solvent week stock relocation 22 is housed in the outlet of the first methyl alcohol separating box 20-1, and methanol tank 21 links to each other with the second methyl alcohol separating box 20-2 through the 3rd condenser 19-3, rectifying tower 23; The said second trap 18-2 links to each other with the 3rd trap 18-3 and solvent pump 25, and links to each other with drag chain leacher 15 through solvent pump 25, and the circulation import of drag chain leacher 15 also links to each other with the second trap 18-2, the 3rd trap 18-3 respectively; The said second methyl alcohol separating box 20-2 is linked to each other with the 4th condenser 19-4 outlet by the circulation import, and the 4th condenser 19-4 links to each other with the 3rd trap 18-3 outlet; The outlet of said the 5th condenser 19-5 links to each other with stock relocation 22 imports of solvent week, and storehouse 22 also links to each other with the outlet of the 6th condenser 19-6, the outlet of water trap 32 respectively around the solvent, and the import of water trap 32 links to each other with the outlet of the 7th condenser 19-7; The outlet of said hybrid oil filter machine 26 links to each other with the second methyl alcohol separating box 20-2 import; Said drag chain leacher 15 is ring-like leacher or flat-turn leacher.
Working condition of the present utility model is,
Deliver among the first lift 2-1 with the cottonseed that feeding pot 1 is returned purchase,, material sent to go out foreign material in the seed cleaner 4 again by the first auger 3-1;
Enter discaling roll Cottonseed shucking machine 5, realize separating of boll hulls and cotton benevolence by angle sieve 6 again, after with wind riddle 7 boll hull being separated then, reclaim by the second auger 3-2, cotton benevolence is then delivered in the horizontal softening kettle 8 by the 3rd auger 3-3, the first lift 2-2 and is softened;
After material is softened,, deliver to pair roller flaker 11 by the first flat scraper conveyor 10-1 by the first scraper conveyor 9-1;
After rolling embryo, material is delivered in the plate dryer 12 by the second flat scraper conveyor 10-2 by the second scraper conveyor 9-2, removes redundant moisture, and then by the 3rd scraper conveyor 9-3, the 3rd flat scraper conveyor 10-3 material is delivered to feed box 13;
Enter among the 4th scraper conveyor 9-4 by feed box, enter in the leaching lattice feed bin in the drag chain leacher 15 by the first sealing auger 14-1, the organic solvent countercurrent spray that circulates from top to bottom leaches and is cottonly delivered among the first drying machine 16-1 by the second sealing auger 14-2 by the 5th scraper conveyor 9-5;
After the first drying machine 16-1, solvent gas is flowed through the first condenser 19-1 in the first methyl alcohol separating box 20-1 by the first trap 18-1, and a part generates methyl alcohol, exists in the methanol tank 21, and a part of solvent is recovered, and flows back in the solvent week stock relocation 22;
Material is delivered among the second drying machine 16-2 by the 3rd sealing auger 14-3 by the 6th scraper conveyor 9-6 through the later leaching cotton of the first drying machine 16-1, solvent vapour enters among the second methyl alcohol separating box 20-2 by the second trap 18-2, dried leaching is cotton to be delivered in the quality-adjusting device 17 by the 4th sealing auger 14-4 by the 7th scraper conveyor 9-7, wherein delivers to dregs of rice storehouse by the 8th scraper conveyor 9-8 by the scraper conveyor 10-4 of Siping City through dried cotton dregs; Mixed gas is by the 3rd wet type trap 18-3, among the 4th condenser 19-4 to the second methyl alcohol separating box 20-2 that flows through;
The mixed gas that comes out from the first long-tube evaportor 27-1 flows back to solvent week stock relocation 22 after the first shwoot case 28-1 is by the 5th condenser 19-5, the mixed gas that comes out from the second long-tube evaportor 27-2 flows back to solvent week stock relocation 22 through the second shwoot case 28-2 by the 6th condenser 19-6, the mixed gas that comes out from disk stripping column 29 flows back to solvent week stock relocation 22 at last by the 7th condenser 19-7 water trap 32 of flowing through, realizes whole from cottonseed the technological process of production dephenolizing protein and Oleum Gossypii semen.
By above-mentioned situation as can be seen, the utility model can be effective to suitability for industrialized production Oleum Gossypii semen, cotton seed dephenolizing protein, the production efficiency height, quality is good, can effectively realize the comprehensive utilization of material, of the present utility model succeeding in developing, overcome the effectively drawback of dephenolize that exists in the cottonseed processing, can effectively solve cottonseed cake (cotton dregs) can only be as the after-product of cottonseed processing industry, is restricted in the use of feed, food service industry, and it applies huge economic and social benefit.
Claims (7)
1, a kind of cottonseed pre-treatment, cotton seed dephenolizing protein complete equipment is produced in extraction, include the feeding pot (1) of serial connection successively, first lift (2-1), first stirs cage (3-1), seed cleaner (4), discaling roll Cottonseed shucking machine (5), angle sieve (6), wind riddle (7), second lift (2-2), horizontal softening kettle (8), first scraper conveyor (9-1), the first flat scraper conveyor (10-1), pair roller flaker (11), second scraper conveyor (9-2), the second flat scraper conveyor (10-2), plate dryer (12), the 3rd scraper conveyor (9-3), the 3rd flat scraper conveyor (10-3), feed box (13) and the 4th scraper conveyor (9-4), it is characterized in that, the 4th scraper conveyor (9-4) stirs cage (14-1) through first sealing and links to each other with drag chain leacher (15) import, be connected to the 5th scraper conveyor (9-5) respectively in three outlets of drag chain leacher (15), hybrid oil filter machine (26) and solvent pump (25), it is continuous with the import of first drying machine (16-1) that the 5th scraper conveyor (9-5) stirs cage (14-2) through second sealing, be connected to the 6th scraper conveyor (9-6) respectively in two outlets of first drying machine (16-1), first trap (18-1), it is continuous with the import of second drying machine (16-2) that the 6th scraper conveyor (9-6) stirs cage (14-3) through the 3rd sealing, two outlets of second drying machine (16-2) are respectively with the 7th scraper conveyor (9-7), the import of second trap (18-2) links to each other, the 7th scraper conveyor (9-7) outlet is stirred cage (14-4) through the 4th sealing and is linked to each other with the import of quality-adjusting device (17), two outlets of quality-adjusting device (17) link to each other with the import of the 8th scraper conveyor (9-8) and the 3rd trap (18-3) respectively, the outlet of the 8th scraper conveyor (9-8) links to each other with the dephenolizing protein stockyard through Siping City's scraper conveyor (10-4), second trap (18-2) links to each other with the second methyl alcohol separating box (20-2) through second condenser (19-2), the second methyl alcohol separating box (20-2) is through miscella tank (24), first long-tube evaportor (27-1) links to each other with the import of the first shwoot case (28-1), be connected to the 5th condenser (19-5) respectively in two outlets of the first shwoot case (28-1), second long-tube evaportor (27-2), second long-tube evaportor (27-2) links to each other with the import of the second shwoot case (28-2), two outlets of the second shwoot case (28-2) are respectively with the 6th condenser (19-6), layer dish stripping tower (29) links to each other, two outlets of layer dish stripping tower (29) are respectively with the 7th condenser (19-7), crude oil jar (30) links to each other, and crude oil jar (30) links to each other with the cotton oil storehouse through oil pump (31).
2, cotton seed dephenolizing protein complete equipment is produced in cottonseed pre-treatment according to claim 1, extraction, it is characterized in that, the second strand cage (3-2) is housed on the pipeline between said angle sieve (6), the wind riddle (7), is provided with the 3rd between wind riddle (7), the 4th strand cage (3-4) and stirs cage (3-3).
3. cotton seed dephenolizing protein complete equipment is produced in cottonseed pre-treatment according to claim 1, extraction, it is characterized in that, said first trap (18-1) outlet links to each other through the import of first condenser (19-1) with the first methyl alcohol separating box (20-1), methanol tank (21) and solvent week stock relocation (22) is housed in the outlet of the first methyl alcohol separating box (20-1), and methanol tank (21) links to each other with the second methyl alcohol separating box (20-2) through the 3rd condenser (19-3), rectifying tower (23).
4, cotton seed dephenolizing protein complete equipment is produced in cottonseed pre-treatment according to claim 1, extraction, it is characterized in that, said second trap (18-2) links to each other with the 3rd trap (18-3) and solvent pump (25), and continuous through solvent pump (25) with drag chain leacher (15), the circulation import of drag chain leacher (15) also links to each other with second trap (18-2), the 3rd trap (18-3) respectively.
5, cotton seed dephenolizing protein complete equipment is produced in cottonseed pre-treatment according to claim 1, extraction, it is characterized in that, the said second methyl alcohol separating box (20-2) is linked to each other with the 4th condenser (19-4) outlet by the circulation import, and the 4th condenser (19-4) links to each other with the 3rd trap (18-3) outlet.
6, cotton seed dephenolizing protein complete equipment is produced in cottonseed pre-treatment according to claim 1, extraction, it is characterized in that, the outlet of said the 5th condenser (19-5) links to each other with stock relocation (22) import of solvent week, storehouse (22) also links to each other with the outlet of the 6th condenser (19-6), the outlet of water trap (32) respectively around the solvent, and the import of water trap (32) links to each other with the outlet of the 7th condenser (19-7).
7, cotton seed dephenolizing protein complete equipment is produced in cottonseed pre-treatment according to claim 1, extraction, it is characterized in that, the outlet of said hybrid oil filter machine (26) links to each other with second methyl alcohol separating box (20-2) import.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200912914U CN201433185Y (en) | 2009-07-03 | 2009-07-03 | Complete sets of equipment for cottonseed pretreatment and extraction production of dephenolization cottonseed protein |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200912914U CN201433185Y (en) | 2009-07-03 | 2009-07-03 | Complete sets of equipment for cottonseed pretreatment and extraction production of dephenolization cottonseed protein |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201433185Y true CN201433185Y (en) | 2010-03-31 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200912914U Expired - Lifetime CN201433185Y (en) | 2009-07-03 | 2009-07-03 | Complete sets of equipment for cottonseed pretreatment and extraction production of dephenolization cottonseed protein |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201433185Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104086622A (en) * | 2014-07-01 | 2014-10-08 | 新疆塔里木震企生物科技有限公司 | Circulating dephenolizing device and circulating dephenolizing process for producing cottonseed protein by virtue of extraction method |
-
2009
- 2009-07-03 CN CN2009200912914U patent/CN201433185Y/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104086622A (en) * | 2014-07-01 | 2014-10-08 | 新疆塔里木震企生物科技有限公司 | Circulating dephenolizing device and circulating dephenolizing process for producing cottonseed protein by virtue of extraction method |
| CN104086622B (en) * | 2014-07-01 | 2017-09-05 | 新疆金谷园生物科技有限公司 | Extraction production cottonseed protein circulation dephenolize device and its technique |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Henan Huatai Grain Machinery Engineering Co., Ltd. Assignor: Beijing Huakang Xiwang Biology Tehcnolgoy Co., Ltd. Contract record no.: 2010410000164 Denomination of utility model: Complete sets of equipment for cottonseed pretreatment and extraction production of dephenolization cottonseed protein Granted publication date: 20100331 License type: Exclusive License Record date: 20101130 |
|
| ASS | Succession or assignment of patent right |
Owner name: HENAN HUATAI GRAIN MACHINERY ENGINEERING CO., LTD. Free format text: FORMER OWNER: BEIJING HUAKANG HOPE BIO-TECHNOLOGY CO., LTD. Effective date: 20120521 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20120521 Address after: 456400 No. 201 Jiefang North Road, Huaxian, Henan Patentee after: Henan Huatai Grain Machinery Engineering Co., Ltd. Address before: 456400 No. 201 Jiefang North Road, Huaxian, Henan Patentee before: Beijing Huakang Xiwang Biology Tehcnolgoy Co., Ltd. |
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| CX01 | Expiry of patent term |
Granted publication date: 20100331 |
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| CX01 | Expiry of patent term |