CN206428171U - A kind of starch liquefacation device for being used to produce resistant dextrin - Google Patents
A kind of starch liquefacation device for being used to produce resistant dextrin Download PDFInfo
- Publication number
- CN206428171U CN206428171U CN201621306373.2U CN201621306373U CN206428171U CN 206428171 U CN206428171 U CN 206428171U CN 201621306373 U CN201621306373 U CN 201621306373U CN 206428171 U CN206428171 U CN 206428171U
- Authority
- CN
- China
- Prior art keywords
- vacuum tank
- oil
- starch liquefacation
- resistant dextrin
- heater
- 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
- 229920002472 Starch Polymers 0.000 title claims abstract description 26
- 235000019698 starch Nutrition 0.000 title claims abstract description 26
- 239000008107 starch Substances 0.000 title claims abstract description 26
- 229920001353 Dextrin Polymers 0.000 title claims abstract description 18
- 239000004375 Dextrin Substances 0.000 title claims abstract description 18
- 235000019425 dextrin Nutrition 0.000 title claims abstract description 18
- 238000002156 mixing Methods 0.000 claims abstract description 21
- 238000009413 insulation Methods 0.000 claims abstract description 6
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 238000007599 discharging Methods 0.000 claims description 7
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 3
- 239000010962 carbon steel Substances 0.000 claims description 3
- 238000001514 detection method Methods 0.000 claims description 3
- 239000000446 fuel Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 239000003153 chemical reaction reagent Substances 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 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 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229920001100 Polydextrose Polymers 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000013325 dietary fiber Nutrition 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000013856 polydextrose Nutrition 0.000 description 1
- 239000001259 polydextrose Substances 0.000 description 1
- 229940035035 polydextrose Drugs 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Cosmetics (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
The utility model discloses a kind of starch liquefacation device for being used to produce resistant dextrin, including base, the upper end of the base is provided with vacuum tank, vacuum tank is from outside to inside successively by outer layer, middle level and internal layer composition, and oil bath chamber is constituted between internal layer and middle level, the starch liquefacation device can be heated by oil bath, and thermal source is placed on the outside of vacuum tank, cold oil and deep fat can just be pumped into oil bath intracavitary when assigned temperature is mixed into blending bin, the uniformity of heating is ensured, outside due to vacuum tank uses thermal insulation ceramicses and vacuum chamber to carry out strictly heat-insulated, therefore, it is possible to the waste for effectively avoiding energy and stable internal temperature, the present apparatus will can also be evacuated by vavuum pump inside device, gaseous reagent is then added by the air inlet pipe of front end, so as to realize to the more preferable liquefaction of starch, there is more preferable function compared to the simple starch liquefacation vacuum tank of traditional structure, practicality is higher.
Description
Technical field
The utility model is related to resistant dextrin processing technique field, specially a kind of starch fluid for being used to produce resistant dextrin
Makeup is put.
Background technology
Resistant dextrin is processed by starch, it may be difficult to a kind of Low Caloric Polydextrose that the composition of digestion refines out,
Belong to low molecule oil-soluble dietary fiber, the primary process of resistant dextrin production is that starch is liquefied, followed in turn by separation
Device carries out separating-purifying, due to starch liquefacation during need to maintain certain temperature, and add corresponding reagent, existing shallow lake
Powder liquefaction process, which is mainly, to be put into vacum reaction tank, but common vacum reaction tank heat-insulating capability is poor, it is not easy to remain internal
Stable environment, a kind of starch liquefacation device for being used to produce resistant dextrin is we provided for this.
The content of the invention
The purpose of this utility model is to provide a kind of starch liquefacation device for being used to produce resistant dextrin, above-mentioned to solve
The problem of being proposed in background technology.
To achieve the above object, the utility model provides following technical scheme：
A kind of starch liquefacation device for being used to produce resistant dextrin, including base, the upper end of the base is provided with vacuum
Tank, the vacuum tank is made up of outer layer, middle level and internal layer successively from outside to inside, and oil bath chamber, institute are constituted between internal layer and middle level
The upper end for stating base is provided with support, and the front end of support is provided with control device, and the rear end of the control device is provided with very
Empty pump, and vavuum pump connects the inner chamber of vacuum tank by vacuum tank, the right-hand member of the control device is provided with blending bin and heating
Device, and the upper end of blending bin is provided with cold oil pipe and flowline, the heater connects blending bin, and heating by oil pipe
Device and blending bin are connected in vacuum chamber, the heater and blending bin by oil pipe and are provided with oil pump, and vacuum tank
Upper end be provided with feed pipe, the lower end of the vacuum tank, which is provided with discharge nozzle, and discharge nozzle, is provided with discharging control valve, institute
State control device and vavuum pump, discharging control valve and heater is electrically connected, and oil bath intracavitary is provided with and control device
The temperature detection sensor of electric connection.
It is preferred that, the upper end of the vacuum tank is provided with the motor being electrically connected with control device, and motor
Lower end driving have an agitating paddle, the motor is stepper motor.
It is preferred that, the front end of the vacuum tank is provided with air inlet pipe, and the front end connection high-pressure pump of air inlet pipe.
It is preferred that, being internally provided between conduction oil, and outer layer and middle level for oil bath chamber is provided with vacuum chamber, described
Outer layer is thermal insulation ceramicses, and middle level is carbon steel.
It is preferred that, the outer wall of the oil bath chamber is provided with temperature-uniforming plate, and the surface of temperature-uniforming plate is provided with mould release membrance.
It is preferred that, the control device is stm32 series monolithics or S7-200 series of PLC devices.
It is preferred that, the heater is the closed fuel reserve tank of built-in resistor heater strip or electromagnetic heater.
Compared with prior art, the beneficial effects of the utility model are：The starch liquefacation device energy of the utility model design
Enough heated by oil bath, and thermal source is placed on the outside of vacuum tank, and cold oil and deep fat are mixed into blending bin specifies temperature
Oil bath intracavitary can be just pumped into when spending, the uniformity of heating has been ensured, outside due to vacuum tank uses thermal insulation ceramicses and vacuum
Chamber has carried out strictly heat-insulated, and therefore, it is possible to the waste for effectively avoiding energy and stable internal temperature, the present apparatus can also lead to
Crossing vavuum pump will be evacuated inside device, then gaseous reagent be added by the air inlet pipe of front end, so as to realize to starch more
Good liquefaction, has more preferable function, practicality is higher compared to the simple starch liquefacation vacuum tank of traditional structure.
Brief description of the drawings
Fig. 1 is the utility model structural representation；
Fig. 2 is the sectional view of the utility model structure.
In figure：1 base, 2 vacuum tanks, 201 outer layers, 202 vacuum chambers, 203 middle levels, 204 oil bath chambers, 205 internal layers, 3 controls
Device, 4 vavuum pumps, 5 cold oil pipes, 6 vacuum tubes, 7 flowlines, 8 agitating paddles, 9 motors, 10 feed pipes, 11 supports, 12 air inlets
Pipe, 13 discharging control valves, 14 discharge nozzles, 15 blending bins, 16 heaters.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belongs to the scope of the utility model protection.
Fig. 1-2 is referred to, the utility model provides a kind of technical scheme：
A kind of starch liquefacation device for being used to produce resistant dextrin, including base 1, the upper end of base 1 is provided with vacuum tank
2, vacuum tank 2 is made up of outer layer 201, middle level 203 and internal layer 205 successively from outside to inside, and structure between internal layer 205 and middle level 203
Into oil bath chamber 204, the upper end of base 1 is provided with support 11, and the front end of support 11 is provided with control device 3, control device 3
Rear end is provided with vavuum pump 4, and vavuum pump 4 connects the inner chamber of vacuum tank 2 by vacuum tube 6, and the right-hand member of control device 3 is provided with
Blending bin 15 and heater 16, and the upper end of blending bin 15 is provided with cold oil pipe 5 and flowline 7, heater 16 passes through oil
Pipe connects blending bin 15, and heater 16 and blending bin 15 connect vacuum chamber 202, heater 16 and mixing by oil pipe
Oil pump is provided with case 15, and the upper end of vacuum tank 2 is provided with feed pipe 10, the lower end of vacuum tank 2 is provided with discharge nozzle 14,
And discharging control valve 13 is provided with discharge nozzle 14, control device 3 is electrically connected vavuum pump 4, discharging control valve 13 and added
The temperature detection sensor being electrically connected with control device 3 is provided with thermal 16, and oil bath chamber 204.
The upper end of vacuum tank 2 is provided with the motor 9 being electrically connected with control device 3, and the lower end of motor 9 is driven
Dynamic to have agitating paddle 8, motor 9 is stepper motor, and the front end of vacuum tank 2 is provided with air inlet pipe 12, and the front end of air inlet pipe 12
High-pressure pump is connected, being internally provided between conduction oil, and outer layer 201 and middle level 203 for oil bath chamber 204 is provided with vacuum chamber
202, outer layer 201 is thermal insulation ceramicses, and middle level 203 is carbon steel, and the outer wall of oil bath chamber 204 is provided with temperature-uniforming plate, and temperature-uniforming plate
Surface is provided with mould release membrance, and control device 3 is stm32 series monolithics or S7-200 series of PLC devices, and heater 16 is
The closed fuel reserve tank of built-in resistor heater strip or electromagnetic heater.
The present apparatus can be heated by oil bath, and thermal source is placed on the outside of vacuum tank 2, and cold oil and deep fat are in mixing
It can just be pumped into oil bath chamber 204, ensured in the uniformity of heating, specific bath chamber 204 when assigned temperature is mixed into case 15
Fluid flow into heater 16 and heat, and mix in blending bin with the cold oil in cold oil pipe 5 so as to be flowed back to by blending bin
Oil bath chamber 204, unnecessary fluid is then discharged by flowline 7, and outside due to vacuum tank 2 is carried out using thermal insulation ceramicses and vacuum chamber
Strict is heat-insulated, and therefore, it is possible to the waste for effectively avoiding energy and stable internal temperature, the present apparatus can also pass through vavuum pump 4
It will be evacuated inside device, gaseous reagent then added by the air inlet pipe 12 of front end, so as to realize to the more preferable liquid of starch
Change, there is more preferable function compared to the simple starch liquefacation vacuum tank of traditional structure, practicality is higher.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out in the case where not departing from principle of the present utility model and spirit a variety of changes, repaiies
Change, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (7)
1. a kind of starch liquefacation device for being used to produce resistant dextrin, including base（1）, it is characterised in that：The base（1）'s
Upper end is provided with vacuum tank（2）, the vacuum tank（2）From outside to inside successively by outer layer（201）, middle level（203）And internal layer（205）
Composition, and internal layer（205）And middle level（203）Between constitute oil bath chamber（204）, the base（1）Upper end be provided with support
（11）, and support（11）Front end be provided with control device（3）, the control device（3）Rear end be provided with vavuum pump（4）,
And vavuum pump（4）Pass through vacuum tube（6）Connect vacuum tank（2）Inner chamber, the control device（3）Right-hand member be provided with blending bin
（15）And heater（16）, and blending bin（15）Upper end be provided with cold oil pipe（5）And flowline（7）, the heater
（16）Blending bin is connected by oil pipe（15）, and heater（16）And blending bin（15）Vacuum chamber is connected by oil pipe
（202）, the heater（16）And blending bin（15）Inside it is provided with oil pump, and vacuum tank（2）Upper end be provided with charging
Pipe（10）, the vacuum tank（2）Lower end be provided with discharge nozzle（14）, and discharge nozzle（14）On be provided with discharging control valve
（13）, the control device（3）Vavuum pump is electrically connected（4）, discharging control valve（13）And heater（16）, and oil bath
Chamber（204）Inside it is provided with and control device（3）The temperature detection sensor of electric connection.
2. a kind of starch liquefacation device for being used to produce resistant dextrin according to claim 1, it is characterised in that：It is described true
Slack tank（2）Upper end be provided with and control device（3）The motor of electric connection（9）, and motor（9）Lower end driving
There is agitating paddle（8）, the motor（9）For stepper motor.
3. a kind of starch liquefacation device for being used to produce resistant dextrin according to claim 1, it is characterised in that：It is described true
Slack tank（2）Front end be provided with air inlet pipe（12）, and air inlet pipe（12）Front end connection high-pressure pump.
4. a kind of starch liquefacation device for being used to produce resistant dextrin according to claim 1, it is characterised in that：The oil
Bathe chamber（204）Be internally provided with conduction oil, and outer layer（201）And middle level（203）Between be provided with vacuum chamber（202）, it is described
Outer layer（201）For thermal insulation ceramicses, and middle level（203）For carbon steel.
5. a kind of starch liquefacation device for being used to produce resistant dextrin according to claim 1, it is characterised in that：The oil
Bathe chamber（204）Outer wall be provided with temperature-uniforming plate, and the surface of temperature-uniforming plate is provided with mould release membrance.
6. a kind of starch liquefacation device for being used to produce resistant dextrin according to claim 1, it is characterised in that：The control
Device processed（3）For stm32 series monolithics or S7-200 series of PLC devices.
7. a kind of starch liquefacation device for being used to produce resistant dextrin according to claim 1, it is characterised in that：It is described to add
Thermal（16）For built-in resistor heater strip or the closed fuel reserve tank of electromagnetic heater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621306373.2U CN206428171U (en) | 2016-12-01 | 2016-12-01 | A kind of starch liquefacation device for being used to produce resistant dextrin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621306373.2U CN206428171U (en) | 2016-12-01 | 2016-12-01 | A kind of starch liquefacation device for being used to produce resistant dextrin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206428171U true CN206428171U (en) | 2017-08-22 |
Family
ID=59586119
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621306373.2U Expired - Fee Related CN206428171U (en) | 2016-12-01 | 2016-12-01 | A kind of starch liquefacation device for being used to produce resistant dextrin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206428171U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115261429A (en) * | 2022-07-18 | 2022-11-01 | 广州双桥股份有限公司 | A kind of liquefaction method of starch |
| CN117003900A (en) * | 2023-07-14 | 2023-11-07 | 江门市英杰特机械设备有限公司 | Reaction tank for producing dextrin from cassava starch by acid method |
-
2016
- 2016-12-01 CN CN201621306373.2U patent/CN206428171U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115261429A (en) * | 2022-07-18 | 2022-11-01 | 广州双桥股份有限公司 | A kind of liquefaction method of starch |
| CN117003900A (en) * | 2023-07-14 | 2023-11-07 | 江门市英杰特机械设备有限公司 | Reaction tank for producing dextrin from cassava starch by acid method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170822 Termination date: 20201201 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |