CN204569791U - A kind of mechanism of by-product piperylene - Google Patents
A kind of mechanism of by-product piperylene Download PDFInfo
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- CN204569791U CN204569791U CN201520199547.9U CN201520199547U CN204569791U CN 204569791 U CN204569791 U CN 204569791U CN 201520199547 U CN201520199547 U CN 201520199547U CN 204569791 U CN204569791 U CN 204569791U
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- piperylene
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Abstract
The utility model discloses a kind of mechanism of by-product piperylene, this device belongs to nonstaple food production field, comprise: rinsing machine, dryer, pulverizer, homogenizer, separating machine, enzymatic vessel, separating centrifuge, it is characterized in that: rinsing machine is provided with wheat import, high pressure water import, washing water export, the first transfer roller is provided with between rinsing machine and dryer, second conveyor is provided with between dryer and pulverizer, the 3rd transfer roller is provided with between pulverizer and homogenizer, homogenizer is provided with water inlet, the first shurry pump and pipeline is provided with between homogenizer and separating machine, separating machine is provided with wheat starch outlet, wheat-gluten exports, the second shurry pump and pipeline is provided with between separating machine and enzymatic vessel, enzymatic vessel is provided with zymin import, soda acid import, the 3rd shurry pump and pipeline is provided with between enzymatic vessel and separating centrifuge, separating centrifuge is provided with piperylene outlet, processing wastewater exports.
Description
Technical field
The utility model belongs to nonstaple food production field, particularly relates to a kind of mechanism taking wheat as by-product piperylene in raw material production wheat-gluten technique.
Background technology
Wheat is a kind of grass in extensively plantation all over the world, and the caryopsis of wheat is one of staple food of the mankind, can make the foods such as bread, steamed bun, biscuit, noodles after wearing into flour; Beer, alcohol, vodka or raw matter fuel is can be made into after fermentation.Wheat rich in starch, protein, fat, mineral substance, calcium, iron, VitB1, riboflavin, nicotinic acid, vitamin A and vitamins C etc.Many kinds of substance can be extracted, as wheat-gluten, wheat starch, piperylene from wheat.The utility model is a kind of device of by-product piperylene, and piperylene is a kind of non-starch polysaccharide, extensively exists in the cereal such as wheat, rye, Chinese sorghum, but content is few, and it is the important component forming plant cell wall.Piperylene improves significantly to the formation of dough and the baking quality of bread; Piperylene has high viscosity, high retention ability, the character such as oxidation cross-linked, can be used as the additive application such as thickening material, wetting Agent for Printing Inks in food system.Piperylene is a kind of well food fibre, cannot be digested in human body, has good function of relaxing bowel; Medically, piperylene also has prevention and corntrol mammary cancer, fat-reducing and effect that is hypotensive, blood sugar; Through further studying discovery, piperylene probably becomes the functional factor of healthcare products of new generation.The utility model is a kind of mechanism of by-product piperylene, this device with rinsing machine, dryer, pulverizer, homogenizer, separating machine, enzymatic vessel, separating centrifuge for equipment, take good quality wheat as raw material, by obtained finished product after the washing of wheat, oven dry, pulverizing, homogeneous, separation, enzymolysis, centrifugation, the major advantage of this device is: the equipment of use is foodstuff production general-purpose equipment, production technique is simple, working condition is gentle, without high temperature and high pressure, and production automation degree is high, good product quality.
Summary of the invention
The problem that the utility model mainly solves is to provide a kind of mechanism of by-product piperylene, and this device carrys out by-product piperylene with rinsing machine, dryer, pulverizer, homogenizer, separating machine, enzymatic vessel, separating centrifuge for equipment.
The technical solution adopted in the utility model is:
A mechanism for by-product piperylene, comprising: rinsing machine 1, dryer 2, pulverizer 3, homogenizer 4, separating machine 5, enzymatic vessel 6, separating centrifuge 7, it is characterized in that: rinsing machine 1 is provided with wheat import 8, high pressure water import 9, washing water outlet 10, the first transfer roller 11 is provided with between rinsing machine 1 and dryer 2, second conveyor 12 is provided with between dryer 2 and pulverizer 3, the 3rd transfer roller 13 is provided with between pulverizer 3 and homogenizer 4, homogenizer 4 is provided with water inlet 14, the first shurry pump and pipeline 15 is provided with between homogenizer 4 and separating machine 5, separating machine 5 is provided with wheat starch outlet 16, wheat-gluten outlet 17, the second shurry pump and pipeline 18 is provided with between separating machine 5 and enzymatic vessel 6, enzymatic vessel 6 is provided with zymin import 19, soda acid import 20, the 3rd shurry pump and pipeline 21 is provided with between enzymatic vessel 6 and separating centrifuge 7, separating centrifuge 7 is provided with piperylene outlet 22, processing wastewater outlet 23.
Further technical scheme of the present utility model is:
Described homogenizer is high pressure homogenizer.
Described separating machine is Three-phase decanter centrifuge.
Described enzymatic vessel is 3000 liters of enzymatic vessels.
First, second, third described transfer roller is scraper conveyor.
First, second, third described shurry pump is stainless steel, and corresponding pipeline is polyethylene material.
The beneficial effects of the utility model are: the mechanism providing a kind of by-product piperylene, this device uses the general-purpose equipment combination of producing food, have that rational in infrastructure, production technique is simple, production automation degree is high, the advantages such as good product quality, product piperylene has high viscosity, high retention ability, the character such as oxidation cross-linked, can be used as the additive application such as thickening material, wetting Agent for Printing Inks in food system.
Accompanying drawing explanation
Fig. 1 is the technological process of production block diagram of the utility model device.
Embodiment
Embodiment:
The particular content using this mechanism by-product piperylene most preferred embodiment is further illustrated below in conjunction with accompanying drawing:
1. wheat is sent into rinsing machine 1 by the wheat import 8 be arranged on rinsing machine 1, send into high pressure water by the high pressure water import 9 be arranged on rinsing machine 1 immediately to rinse wheat, all impurity of removing wheat grain outside surface, washing water are discharged by the washing water outlet 10 be arranged on rinsing machine 1; Clean wheat is sent into dryer 2 by the first transfer roller 11 be arranged between rinsing machine 1 and dryer 2, after drying the moisture contained by wheat, immediately it is sent into pulverizer 3 by the second conveyor 12 be arranged between dryer 2 and pulverizer 3 and pulverize as powder.
2. wheat powder is sent into homogenizer 4 by the 3rd transfer roller 13 be arranged between pulverizer 3 and homogenizer 4, first added the water of formula ratio by the water inlet 14 be arranged on homogenizer 4, the homogeneous one-tenth mashed prod of the laggard horizontal high voltage that stirs; By mashed prod by being arranged at the first shurry pump between homogenizer 4 and separating machine 5 and separating machine 5 sent into by pipeline 15, separating machine 5 is by first separating piperylene with different rotating speeds; Then by starch separation out, starch discharges recycling by the starch outlet 16 be arranged on separating machine 5; Again wheat-gluten is separated, it is discharged recycling by the wheat-gluten outlet 17 be arranged on separating machine 5; Piperylene is by being arranged at the second shurry pump between separating machine 5 and enzymatic vessel 6 and enzymatic vessel 6 sent into by pipeline 18; Then the zymin of formula ratio is added by the zymin import 19 be arranged on enzymatic vessel 6, then adding appropriate soda acid by the soda acid import 20 be arranged on enzymatic vessel 6 adjusts the pH value of liquid in tank to be 7-8, temperature is 55 DEG C, and the enzymolysis that stirs stopped enzymolysis obtaining zymolyte after 3 hours.
3. zymolyte is sent into separating centrifuge 7 and carried out centrifugal solid-liquid by being arranged at the 3rd shurry pump between enzymatic vessel 6 with separating centrifuge 7 and pipeline 21 and be separated, isolated solid is piperylene, packaging is discharged by the piperylene outlet 22 be arranged on separating centrifuge 7, liquid portion is processing wastewater, discharges simmer down to feed by the processing wastewater outlet 23 be arranged on separating centrifuge 7.
Certainly, the utility model also has other embodiment, not leaving the improvement of any technology, principle and the technique done under spiritual background of the present utility model, all drops within protection domain of the present utility model.
Claims (6)
1. a mechanism for by-product piperylene, comprising: rinsing machine (1), dryer (2), pulverizer (3), homogenizer (4), separating machine (5), enzymatic vessel (6), separating centrifuge (7), it is characterized in that: rinsing machine (1) is provided with wheat import (8), high pressure water import (9), washing water outlet (10), the first transfer roller (11) is provided with between rinsing machine (1) and dryer (2), second conveyor (12) is provided with between dryer (2) and pulverizer (3), the 3rd transfer roller (13) is provided with between pulverizer (3) and homogenizer (4), homogenizer (4) is provided with water inlet (14), the first shurry pump and pipeline (15) is provided with between homogenizer (4) and separating machine (5), separating machine (5) is provided with wheat starch outlet (16), wheat-gluten outlet (17), the second shurry pump and pipeline (18) is provided with between separating machine (5) and enzymatic vessel (6), enzymatic vessel (6) is provided with zymin import (19), soda acid import (20), the 3rd shurry pump and pipeline (21) is provided with between enzymatic vessel (6) and separating centrifuge (7), separating centrifuge (7) is provided with piperylene outlet (22), processing wastewater outlet (23).
2. the mechanism of a kind of by-product piperylene according to claim 1, is characterized in that: described homogenizer is high pressure homogenizer.
3. the mechanism of a kind of by-product piperylene according to claim 1, is characterized in that: described separating machine is Three-phase decanter centrifuge.
4. the mechanism of a kind of by-product piperylene according to claim 1, is characterized in that: described enzymatic vessel is 3000 liters of enzymatic vessels.
5. the mechanism of a kind of by-product piperylene according to claim 1, is characterized in that: first, second, third described transfer roller is scraper conveyor.
6. the mechanism of a kind of by-product piperylene according to claim 1, is characterized in that: first, second, third described shurry pump is stainless steel, and corresponding pipeline is polyethylene material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520199547.9U CN204569791U (en) | 2015-04-05 | 2015-04-05 | A kind of mechanism of by-product piperylene |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520199547.9U CN204569791U (en) | 2015-04-05 | 2015-04-05 | A kind of mechanism of by-product piperylene |
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| CN204569791U true CN204569791U (en) | 2015-08-19 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520199547.9U Expired - Fee Related CN204569791U (en) | 2015-04-05 | 2015-04-05 | A kind of mechanism of by-product piperylene |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114933664A (en) * | 2022-06-14 | 2022-08-23 | 河南飞天生物科技股份有限公司 | Extraction method of pentosan |
| CN115181189A (en) * | 2022-07-26 | 2022-10-14 | 河南飞天生物科技股份有限公司 | Method and system for co-producing pentosan by resistant dextrin |
-
2015
- 2015-04-05 CN CN201520199547.9U patent/CN204569791U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114933664A (en) * | 2022-06-14 | 2022-08-23 | 河南飞天生物科技股份有限公司 | Extraction method of pentosan |
| CN115181189A (en) * | 2022-07-26 | 2022-10-14 | 河南飞天生物科技股份有限公司 | Method and system for co-producing pentosan by resistant dextrin |
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| Date | Code | Title | Description |
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| 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: 20150819 Termination date: 20180405 |
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| CF01 | Termination of patent right due to non-payment of annual fee |