CN219816232U - Production system of polydextrose - Google Patents
Production system of polydextrose Download PDFInfo
- Publication number
- CN219816232U CN219816232U CN202320751420.8U CN202320751420U CN219816232U CN 219816232 U CN219816232 U CN 219816232U CN 202320751420 U CN202320751420 U CN 202320751420U CN 219816232 U CN219816232 U CN 219816232U
- Authority
- CN
- China
- Prior art keywords
- storage tank
- production system
- polydextrose
- fluidized bed
- sorbitol
- 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.)
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- DLRVVLDZNNYCBX-UHFFFAOYSA-N Polydextrose Polymers OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(O)O1 DLRVVLDZNNYCBX-UHFFFAOYSA-N 0.000 title claims abstract description 60
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 31
- 229920001100 Polydextrose Polymers 0.000 title claims abstract description 30
- 239000001259 polydextrose Substances 0.000 title claims abstract description 30
- 229940035035 polydextrose Drugs 0.000 title claims abstract description 30
- 235000013856 polydextrose Nutrition 0.000 title claims abstract description 30
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 238000002156 mixing Methods 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 claims abstract description 4
- 238000003860 storage Methods 0.000 claims description 33
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 claims description 30
- 239000000600 sorbitol Substances 0.000 claims description 30
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 22
- 238000001816 cooling Methods 0.000 claims description 16
- 238000004806 packaging method and process Methods 0.000 claims description 10
- 239000008103 glucose Substances 0.000 claims description 9
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 3
- 230000008569 process Effects 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract 1
- 239000000047 product Substances 0.000 description 33
- 239000000463 material Substances 0.000 description 6
- 238000006116 polymerization reaction Methods 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 206010010774 Constipation Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013325 dietary fiber Nutrition 0.000 description 1
- 210000002249 digestive system Anatomy 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000007102 metabolic function Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
The utility model provides a polydextrose production system which comprises a high-speed mixer, a reaction kettle, an air-cooled fluidized bed, a pulverizer, a salon and a vibrating screen, wherein the high-speed mixer is used for uniformly mixing raw materials, a discharge port pipeline of the high-speed mixer is connected to an inlet of the reaction kettle, a discharge port pipeline of the reaction kettle is connected to the air-cooled fluidized bed, an outlet of the air-cooled fluidized bed is connected to the pulverizer, an outlet pipeline of the pulverizer is connected to the salon, an outlet pipeline of the salon is connected to the vibrating screen, and an outlet of the vibrating screen is used for obtaining polydextrose. The whole process pipeline is simple, compact and reasonable, the product quality is superior to that of similar products, and the energy consumption index is obviously lower than that of similar products.
Description
Technical Field
The utility model relates to the field of polydextrose production, in particular to a polydextrose production system.
Background
The polydextrose is a food additive with health care function, can supplement water-soluble dietary fiber required by human body, and can generate special metabolism function after entering human digestive system, thereby preventing constipation and fat precipitation.
In the existing process of producing polydextrose, intermittent production mode is often adopted for production, namely: after the production of the polydextrose liquid is completed, the polydextrose liquid is manually separated and conveyed by using a small container, and is naturally cooled at normal temperature and then crushed. The production mode has the advantages of high labor cost, high working strength, long production time and low working efficiency, and the production process pipelines with some designs are complex, various devices are more, so that the consumption of steam, electric power and the like is often doubled, the operation cost of enterprises is increased, and the energy waste is caused.
Disclosure of Invention
Aiming at the defects of the prior art, the utility model provides a polydextrose production system which can realize continuous production, greatly improve the production efficiency, save a large amount of manpower and material resources and bring considerable economic benefit to production enterprises.
The technical scheme provided by the utility model is as follows: the utility model provides a production system of polydextrose, includes high-speed blendor, reation kettle, forced air cooling fluidized bed, rubbing crusher, salulone and shale shaker, high-speed blendor is used for evenly mixing the raw materials, and the discharge gate pipe connection of high-speed blendor is to reation kettle's import, and reation kettle's discharge gate pipe connection is to forced air cooling fluidized bed, and the exit linkage of forced air cooling fluidized bed is to rubbing crusher, and rubbing crusher's exit pipeline is connected to salulone, and salulone's exit pipeline is connected to the shale shaker, the export of shale shaker obtains product polydextrose.
Further, a sorbitol feed inlet, a glucose feed inlet and a citric acid feed inlet are respectively arranged on the high-speed mixer, and the sorbitol feed inlet is connected with the liquid sorbitol feed system.
Further, the liquid sorbitol feed system comprises a sorbitol storage tank, wherein a lower pipeline of the sorbitol storage tank is connected to an inlet of a discharge pump, an outlet pipeline of the discharge pump is connected to an inlet of a high-level storage tank, and an outlet pipeline of the high-level storage tank is connected to a high-speed mixer.
Further, the exhaust port of the reaction kettle is connected to a vacuum pump, and the heating port of the reaction kettle is connected to a heat conduction oil heating system.
Further, the inside of forced air cooling fluidized bed communicates with the export of fan, is provided with air cleaner on the import pipeline of fan for carry clean cold air to the inside of forced air cooling fluidized bed through the fan and carry out the rapid cooling to the polydextrose liquid.
Further, the production system further comprises a product storage tank and a packaging machine, wherein an outlet of the vibrating screen is connected to the product storage tank, and an outlet of the product storage tank is connected to the product packaging machine.
Further, the high-level storage tank is provided with a liquid level meter, and the volume of the high-level storage tank is consistent with the consumption of sorbitol added every time.
Further, a stirring device is arranged in the reaction kettle.
The utility model has the beneficial effects that:
(1) The utility model adopts liquid sorbitol to produce the polydextrose, greatly reduces the production cost, adopts a high-speed mixer to mix the sorbitol with the glucose, the citric acid and the like at a high speed, ensures that the product is more thorough in polymerization reaction, has more uniform reaction, improves the purity of the product, and ensures the stability of the quality of the product.
(2) According to the utility model, an air cooling system is adopted for cooling the product, an air filter is added, so that the air quality of cold air can be ensured, meanwhile, the polydextrose is cooled in multiple directions and multiple sections, the product is cooled rapidly while the sanitation index of the product is ensured, and the productivity is greatly improved.
(3) According to the utility model, cyclone separation is added in the product crushing stage, so that the product is cooled again before being packaged, the stability of the product quality is ensured, and meanwhile, the product is screened by adopting a vibrating screen when entering a packaging storage tank, and the product quality is ensured.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
in the figure: 1-external pipelines, 2-liquid sorbitol storage tanks, 3-discharge pumps, 4-high-level storage tanks, 5-glucose feed inlets, 6-citric acid feed inlets, 7-high-speed blendors, 8-reaction kettles, 9-air-cooled fluidized beds, 10-air filters, 11-fans, 12-pulverizers, 13-salons, 14-vibrating screens, 15-product storage tanks, 16-packing machines, 17-conduction oil heating systems and 18-vacuum pumps.
Detailed Description
The present utility model will be further described with reference to the following detailed description, wherein the drawings are for illustrative purposes only and are shown in schematic, rather than physical, drawings, and are not to be construed as limiting the utility model, and wherein certain components of the drawings are omitted, enlarged or reduced in size, and do not represent the actual product size, so it will be understood by those skilled in the art that certain well-known structures in the drawings and descriptions thereof may be omitted, and that all other embodiments obtained by those of ordinary skill in the art without making inventive efforts, based on the embodiments of the present utility model, are within the scope of protection of the present utility model.
In the description of the present utility model, it should be noted that the azimuth or positional relationship indicated by the terms "front", "rear", "upper", "lower", etc. are based on the azimuth or positional relationship shown in the drawings, and are merely for convenience of describing the present utility model and simplifying the description, and do not indicate or imply that the apparatus or element referred to must have a specific azimuth, be configured and operated in a specific azimuth, and thus should not be construed as limiting the present utility model.
In the description of the present utility model, it should be noted that, unless explicitly specified and limited otherwise, the terms "mounted," "provided," "connected," and the like are to be construed broadly, and may be either fixedly connected, detachably connected, or integrally connected, for example; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present utility model will be understood in specific cases by those of ordinary skill in the art.
The production system of the polydextrose shown in fig. 1 comprises a high-speed mixer 7, a reaction kettle 8, an air-cooled fluidized bed 9, a pulverizer 12, a salon 13 and a vibrating screen 14, wherein the high-speed mixer 7 is used for uniformly mixing raw materials, a discharge port pipeline of the high-speed mixer 7 is connected to an inlet of the reaction kettle 8, a discharge port pipeline of the reaction kettle 8 is connected to the air-cooled fluidized bed 9, an outlet of the air-cooled fluidized bed 9 is connected to the pulverizer 12, an outlet pipeline of the pulverizer 12 is connected to the salon 13, an outlet pipeline of the salon 13 is connected to the vibrating screen 14, and the outlet of the vibrating screen 14 is used for obtaining the polydextrose product.
And a sorbitol feed inlet, a glucose feed inlet 5 and a citric acid feed inlet 6 are respectively arranged on the high-speed mixer 7, and the sorbitol feed inlet is connected with a liquid sorbitol feed system.
The liquid sorbitol feed system comprises a sorbitol storage tank 2, wherein a lower pipeline of the sorbitol storage tank 2 is connected to an inlet of a discharge pump 3, an outlet pipeline of the discharge pump 3 is connected to an inlet of a high-level storage tank 4, and an outlet pipeline of the high-level storage tank 4 is connected to a sorbitol feed inlet of a high-speed mixer 7.
The exhaust port of the reaction kettle 8 is connected to a vacuum pump 18, and the heating port of the reaction kettle 8 is connected to a heat conduction oil heating system 17.
The inside of the air-cooled fluidized bed 9 is communicated with the outlet of the fan 11, and an air filter 10 is arranged on the inlet pipeline of the fan 11 and is used for conveying clean cold air to the inside of the air-cooled fluidized bed 9 through the fan 11 to rapidly cool the polydextrose liquid.
The production system further comprises a product tank 15 and a packaging machine 16, the outlet of the vibrating screen 14 being connected to the product tank 15, the outlet of the product tank 15 being connected to the product packaging machine 16.
The high-level storage tank 4 is provided with a liquid level meter, and a stirring device is arranged in the reaction kettle 8.
The high-speed mixer is used for fully mixing sorbitol with glucose, citric acid and the like, so that the mixing effect can be better ensured, the polymerization time is shortened, and the stability of the product quality is ensured.
The product of the utility model is cooled and then enters a pulverizer to be pulverized, and then is sent into a saxophone to be cyclone-separated, so that the heat of the product can be reduced again, and the product is ensured to belong to normal-temperature packaging when entering a packaging stage. Products enter the vibrating screen for screening after cyclone separation, so that large particulate matters can be effectively removed, and the fineness of the products is ensured.
In the specific use of the utility model, the pipeline 1 from the previous procedure is connected to a sorbitol storage tank 2, or outsourced liquid sorbitol is put into the sorbitol storage tank 2, and the lower pipeline of the feeding storage tank 2 is connected to a discharge pump 3. The discharging pump 3 is started, liquid sorbitol is conveyed to the high-level storage tank 4 through a pipeline, the volume of the high-level storage tank 4 is equal to the amount of adjustment of each time, glucose and citric acid are respectively put into the high-speed mixer 7 through the glucose feeding port 5 and the citric acid feeding port 6, the liquid sorbitol is put into the high-speed mixer 7 through the high-level storage tank 4, the high-speed mixer 7 is started, and the mixture of glucose and the like is fully mixed and evenly distributed in the mixer. After the high-speed mixer 7 is fully mixed, a discharging valve is opened, and the mixed materials are placed into a reaction kettle 8 through a pipeline. And starting the stirring device of the reaction kettle, simultaneously starting the conduction oil heating system 17 of the reaction kettle to preheat, and simultaneously starting the vacuum pump 18 to ensure that the inside of the reaction kettle 8 is in a negative pressure state.
The reaction kettle 8 is internally provided with stirring continuously, polymerization reaction is promoted, after polymerization reaction of materials in the reaction kettle 8 is completed, a discharge valve of the reaction kettle is opened, the materials are discharged into the air-cooled fluidized bed 9, before the materials enter the fluidized bed system, a fan 11 is required to be started, the air-cooled cooling is carried out on the whole fluidized bed, clean cold air is conveyed into the fluidized bed through the fan 11 to rapidly cool polydextrose liquid, the polydextrose liquid is rapidly coagulated into blocks after being rapidly cooled in multiple directions, the polydextrose liquid enters a pulverizer 12 through a conveying belt in the air-cooled fluidized bed 9, the pulverizer 12 pulverizes the blocky polydextrose into powder, then the powder is conveyed into a cyclone 13 through pneumatic conveying to carry out cyclone separation cooling, the cooled polydextrose product enters a vibrating screen 14 to screen large-particle unsuitable products, and the qualified polydextrose product enters a product storage tank 15 and then enters a packaging machine 16.
The whole polydextrose production system is compact in connection, the production efficiency is greatly improved, a large amount of manpower and material resources are saved, considerable economic benefits can be brought to production enterprises, meanwhile, the on-site environment is convenient to keep clean, and a good working environment is created.
The above description is merely illustrative of specific embodiments of the utility model and is not intended to limit the utility model, but any modifications, equivalents, improvements or alternatives falling within the spirit and scope of the utility model are intended to be included within the scope of the utility model.
Claims (8)
1. A polydextrose production system, characterized in that: including high-speed blendor (7), reation kettle (8), forced air cooling fluidized bed (9), rubbing crusher (12), saxophone (13) and shale shaker (14), high-speed blendor (7) are used for evenly mixing the raw materials, and the exit slot pipe way of high-speed blendor (7) is connected to the import of reation kettle (8), and the exit slot pipe way of reation kettle (8) is connected to forced air cooling fluidized bed (9), and the export of forced air cooling fluidized bed (9) is connected to rubbing crusher (12), and the exit slot of rubbing crusher (12) is connected to saxophone (13), and the exit slot of saxophone (13) is connected to shale shaker (14), the export of shale shaker (14) obtains product polydextrose.
2. The polyglucose production system of claim 1, wherein: the high-speed mixer (7) is respectively provided with a sorbitol feed inlet, a glucose feed inlet (5) and a citric acid feed inlet (6), and the sorbitol feed inlet is connected with a liquid sorbitol feed system.
3. The polyglucose production system of claim 2, wherein: the liquid sorbitol feed system comprises a sorbitol storage tank (2), wherein a lower pipeline of the sorbitol storage tank (2) is connected to an inlet of a discharge pump (3), an outlet pipeline of the discharge pump (3) is connected to an inlet of a high-level storage tank (4), and an outlet pipeline of the high-level storage tank (4) is connected to a sorbitol feed inlet of a high-speed mixer (7).
4. The polyglucose production system of claim 1, wherein: the exhaust port of the reaction kettle (8) is connected to a vacuum pump (18), and the heating port of the reaction kettle (8) is connected to a heat conduction oil heating system (17).
5. The polyglucose production system of claim 1, wherein: the inside of forced air cooling fluidized bed (9) is connected with the export of fan (11), is provided with air cleaner (10) on the import pipeline of fan (11) for carry the inside of forced air cooling fluidized bed (9) through fan (11) with clean cold air and carry out the rapid cooling to the polydextrose liquid.
6. The polyglucose production system of claim 1, wherein: the production system further comprises a product storage tank (15) and a packaging machine (16), wherein the outlet of the vibrating screen (14) is connected to the product storage tank (15), and the outlet of the product storage tank (15) is connected to the product packaging machine (16).
7. A polydextrose production system according to claim 3 characterised in that: the high-level storage tank (4) is provided with a liquid level meter.
8. The polyglucose production system of claim 1, wherein: and a stirring device is arranged in the reaction kettle (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320751420.8U CN219816232U (en) | 2023-04-07 | 2023-04-07 | Production system of polydextrose |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320751420.8U CN219816232U (en) | 2023-04-07 | 2023-04-07 | Production system of polydextrose |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219816232U true CN219816232U (en) | 2023-10-13 |
Family
ID=88249618
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320751420.8U Active CN219816232U (en) | 2023-04-07 | 2023-04-07 | Production system of polydextrose |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219816232U (en) |
-
2023
- 2023-04-07 CN CN202320751420.8U patent/CN219816232U/en active Active
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| GR01 | Patent grant |