CN208927950U - Continuous colloidal sol system - Google Patents
Continuous colloidal sol system Download PDFInfo
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- CN208927950U CN208927950U CN201821544075.6U CN201821544075U CN208927950U CN 208927950 U CN208927950 U CN 208927950U CN 201821544075 U CN201821544075 U CN 201821544075U CN 208927950 U CN208927950 U CN 208927950U
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- colloidal sol
- emulsification pretreatment
- waterworks
- sol system
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Abstract
The utility model relates to colloidal sol fields, relate to a kind of continuous colloidal sol system, its waterworks adjusts the temperature of process water by temperature sensor and regulating valve, flow measurement device can detect that the flow of process water, blanking device then controls the blanking velocity of rubber powder by discharge, process water and rubber powder are mixed in emulsification pretreatment device and are sheared uniformly, enable rubber powder to be rapidly and continuously dissolved into glue, glue is collected and stored to use to food processing by storage device.
Description
Technical field
The utility model relates to colloidal sol fields, more particularly to a kind of continuous colloidal sol system.
Background technique
For food service industry when dissolving xanthan gum, yield is lower, generally has mechanical agitator tank body to dissolve Huang using mini zone
Virgin rubber powder；It is verified, when meltage becomes larger, if directlying adopt biggish dissolving tank to dissolve xanthan gum, it may appear that part is yellow
Virgin rubber conglomeration forms micelle, causes entire glue system uneven, quantifying for glue can not be carried out during food production
Addition.Currently, the technology mode of dissolution glue class material, which mainly uses in canned, is directly stirred shearing to material aqueous mixtures,
Use can be just fed after rubber powder is dissolved completely in water.But xanthan gum material is dissolved using above-mentioned process equipment, is easy to appear office
Portion's conglomeration leads to the problem of micelle, and is influenced by dissolution evenness difference, and traditional dissolution equipment single batch meltage is small, molten
The solution time is long, causes production efficiency low, far can not meet the production requirement of high efficiency mass production.In addition, because rubber powder exists
The production method of stirring and dissolving, which does not have continuity, in tank influences scale metaplasia so the interval time between multiple batches of is longer
The continuity of production, it is higher to eventually lead to production cost.
Utility model content
To solve the above-mentioned problems, existing molten to solve the purpose of the utility model is to provide a kind of continuous colloidal sol system
Gluing equipment can not high-volume continuous-dissolution rubber powder the problem of.
Based on this, the utility model provides a kind of continuous colloidal sol system, including waterworks, blanking device, shearing cream
Makeup is set and storage device, and the waterworks and blanking device are connected to two chargings of the emulsification pretreatment device
End, the discharge end of the emulsification pretreatment device are connected to the storage device；The waterworks include cold water source, thermal water source with
And the regulating valve of the feedwater flow for adjusting the cold water source or thermal water source, the cold water source and thermal water source are connected in parallel and two
The discharge ends of person are connected to temperature sensor, and the temperature sensor is electrically connected at the regulating valve；The waterworks and
The flow measurement device for detecting the technique water flow of waterworks, the blanking device packet are equipped between emulsification pretreatment device
Include the discharge for controlling rubber powder blanking velocity.
Preferably, the waterworks further include water storage device, the water inlet end of the water storage device is connected to described
Cold water source and thermal water source, water outlet are connected to the emulsification pretreatment device by the first liquid pumping device.
Preferably, first liquid pumping device is electrically connected at the flow measurement device, the flow measurement dress
Set the working condition that first liquid pumping device is adjusted according to preset pump liquid flow value.
Preferably, the blanking device further includes the feed bin for containing rubber powder, the discharge end connection of the feed bin
In being additionally provided with feeding port in the discharge, the feed bin.
Preferably, being additionally provided with exhaust blower on the blanking device, the air intake and feeding port of the exhaust blower are adjacent
Setting.
Preferably, being equipped with baiting valve between the discharge and emulsification pretreatment device, the baiting valve is given described
Water installations open when reaching a preset pump liquid flow value and discharge rubber powder.
Preferably, on the storage device have agitating device, the agitating device include stirring driver and
It is connected to the stirring driver and the mixing part of glue is protruded into one end.
Preferably, the feed end that the emulsification pretreatment device is connected to the waterworks is equipped with the first valve,
The discharge end of the emulsification pretreatment device is equipped with the second valve.
Preferably, being equipped with the second liquid pumping device between the emulsification pretreatment device and storage device.
Preferably, the bottom of storage device structure funnel-shaped and there is the blow-off valve that communicates therewith.
The continuous colloidal sol system of the utility model, waterworks adjust process water by temperature sensor and regulating valve
Temperature, flow measurement device can detect that the flow of process water, and blanking device then passes through the blanking speed that discharge controls rubber powder
Degree, process water and rubber powder are mixed in emulsification pretreatment device and are sheared uniformly, enable rubber powder by rapidly and continuously molten
Glue is collected and is stored to use to food processing at glue, storage device by solution.
Detailed description of the invention
Fig. 1 is the overall structure diagram of the continuous colloidal sol system of the utility model embodiment；
Fig. 2 is the structural schematic diagram of the waterworks of the continuous colloidal sol system of the utility model embodiment；
Fig. 3 is the structural schematic diagram of the blanking device of the continuous colloidal sol system of the utility model embodiment；
Fig. 4 is the structural schematic diagram of the storage device of the continuous colloidal sol system of the utility model embodiment.
Wherein, 1, waterworks；11, cold water source；12, thermal water source；13, regulating valve；14, temperature sensor；15, main water
Pipe；16, water storage device；17, the first liquid pumping device；2, blanking device；21, discharge；22, feed bin；221, feeding port；23, it arranges
Blower；24, baiting valve；3, emulsification pretreatment device；31, the first valve；32, the second valve；4, storage device；41, agitating device；
411, driver is stirred；412, mixing part；42, the second liquid pumping device；43, blow-off valve；5, flow measurement device.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Below
Embodiment is not intended to limit the scope of the present invention for illustrating the utility model.
In connection with Figures 1 to 4, schematically show the continuous colloidal sol system of the utility model, including waterworks 1,
Blanking device 2, emulsification pretreatment device 3 and storage device 4, wherein emulsification pretreatment device 3 is preferably high speed shear pump.In conjunction with Fig. 1
With shown in Fig. 2, waterworks 1 and blanking device 2 are connected to two feed ends of emulsification pretreatment device 3, specifically, shearing
Emulsifier unit 3 has liquid feedstock end and feeding-in solid body end, and waterworks 1 are connected to the liquid feedstock end of emulsification pretreatment device 3,
And blanking device 2 is connected to the solid liquid feeding end of emulsification pretreatment device 3.The discharge end of emulsification pretreatment device 3 is for being discharged solid-liquid
Mixture, and the discharge end is connected to storage device 4.In order to provide the process water of suitable temperature and desired flow, waterworks 1
Including cold water source 11, thermal water source 12 and regulating valve 13, in the present embodiment, regulating valve 13 be used to adjust cold water source 11 to water flow
Amount, the i.e. water inlet end of regulating valve 13 are connected to cold water source 11；Cold water source 11 and thermal water source 12 are connected in parallel on water main 15, cold water source
The hot water in 11 hot water or cold water source 12 is mixed into process water, and the temperature that characterization processes water water temperature is parallel on water main 15 passes
Sensor 14, temperature sensor 14 are electrically connected at regulating valve 13, and the water temperature in 14 real-time detection water main 15 of temperature sensor is simultaneously
It is compared with 55 DEG C of preset temperature value, 13 body of process water temperature regulator that regulating valve 13 is detected according to temperature sensor 14 is opened
Degree, and then the process water water temperature in water main 15 is made to be maintained at preset temperature value, meet production requirement.Waterworks 1 and shearing
The flow measurement device 5 for detecting the technique water flow of waterworks 1 is equipped between emulsifier unit 3, maintenance personnel can pass through
Flow measurement device 5 recognizes the flow of current process water.Meanwhile blanking device 2 includes for controlling rubber powder blanking velocity
Discharge 21, such as Fig. 3, it is preferred that discharge 21 is rotary valve.Process water and rubber powder are admitted to shearing cream according to a certain percentage
Makeup sets 3 and mixes shearing uniformly, and rubber powder is enable rapidly and continuously to be dissolved into glue, and final glue is from emulsification pretreatment device
3 discharge end is discharged into storage device 4, in case food processing uses.Such as Fig. 4, there is agitating device 41, stirring on storage device 4
Device 41 includes stirring driver 411 and is connected to stirring driver 411 and the mixing part 412 of glue is protruded into one end, stirring
Portion 412 futher stirs dispersion glue under the driving of stirring driver 411, uneven to prevent local gelatin concentration or tie
Block phenomenon.
In order to enable waterworks 1 steadily to provide process water, waterworks 1 further include water storage device 16, preferably
Water tank.As shown in Fig. 2, the water inlet end of water storage device 16 is connected to water main 15, i.e. cold water source 11 and thermal water source 12 mixes shape
At process water be transported in water storage device 16 and keep in, the water outlet of water storage device 16 is connected to by the first liquid pumping device 17
Emulsification pretreatment device 3, the process water in water storage device 16 is pumped into emulsification pretreatment device 3 by the first liquid pumping device 17, to prevent cold water
The flowed fluctuation of source 11 or thermal water source 12 influence the quality of glue.Further, the first liquid pumping device 17 is electrically connected at stream
Metering device 5 is measured, flow measurement device 5 adjusts the working condition of the first liquid pumping device 17, tool according to preset pump liquid flow value
Body, the technique water flow of the feed end of 5 real-time detection emulsification pretreatment device 3 of flow measurement device, and and preset flow value into
Row compares, and then adjusts the working frequency of the frequency converter of the first liquid pumping device 17.
As shown in connection with fig. 3, blanking device 2 includes feed bin 22 for containing rubber powder again, the structure funnel-shaped of feed bin 22,
Discharge end is connected to discharge 21, and the top of feed bin 22 also has feeding port 221, feeding port of the staff from feed bin 22
221 investment rubber powders, rubber powder is fallen into discharge 21 from the discharge end of 22 bottom of feed bin under gravity, to prevent rubber powder from throwing
The dust recycling generated when putting is additionally provided with exhaust blower 23 on blanking device 2, air intake and 221 phase of feeding port of the exhaust blower 23
Neighbour's setting, to adsorb the dust near feeding port 221.Baiting valve 24 is equipped between discharge 21 and emulsification pretreatment device 3, when giving
After the process water that water installations 1 provide reaches preset pump liquid flow value, baiting valve 24 is opened and rubber powder is discharged into emulsification pretreatment
In device 3.
In addition, the feed end that emulsification pretreatment device 3 is connected to waterworks 1 is equipped with the first valve 31, emulsification pretreatment dress
The discharge end for setting 3 is equipped with the second valve 32, as Fig. 1 closes baiting valve in disassembly, cleaning or maintenance emulsification pretreatment device 3
24, emulsification pretreatment device 3 can be cut off removing by the first valve 31 and the second valve 32 from the system.Emulsification pretreatment device 3
The second liquid pumping device 42, the glue that emulsification pretreatment device 3 can be discharged for the second liquid pumping device 42 are additionally provided between storage device 4
It is actively pumped in storage device 4, so that the mixing shearing work of emulsification pretreatment device 3 is more smooth.In order to by storage device 4
In glue discharge for food processing use, the bottom of storage device 4 structure funnel-shaped and there is the discharge that communicates therewith
Valve 43, opening blow-off valve 43, the glue in storage device 4 can be discharged.
In conclusion continuous colloidal sol system, waterworks 1 adjust technique by temperature sensor 14 and regulating valve 13
The temperature of water, flow measurement device 5 can detect that the flow of process water, blanking device 2 then control rubber powder by discharge 21
Blanking velocity, process water and rubber powder are mixed in emulsification pretreatment device 3 and are sheared uniformly, enable rubber powder by quickly and even
It is dissolved into glue continuously, glue is collected and stored to use to food processing by storage device 4.
The above is only the preferred embodiment of the utility model, it is noted that for the common skill of the art
For art personnel, without deviating from the technical principle of the utility model, several improvement and replacement can also be made, these change
It also should be regarded as the protection scope of the utility model into replacement.
Claims (10)
1. a kind of continuous colloidal sol system, which is characterized in that filled including waterworks, blanking device, emulsification pretreatment device and storing
It sets, the waterworks and blanking device are connected to two feed ends of the emulsification pretreatment device, the emulsification pretreatment
The discharge end of device is connected to the storage device；The waterworks include cold water source, thermal water source and described for adjusting
The regulating valve of cold water source or the feedwater flow of thermal water source, the cold water source is connected in parallel with thermal water source and the discharge ends of the two are connected to
In temperature sensor, the temperature sensor is electrically connected at the regulating valve；The waterworks and emulsification pretreatment device it
Between be equipped with flow measurement device for detecting the technique water flow of waterworks, the blanking device includes for controlling rubber powder
The discharge of blanking velocity.
2. continuous colloidal sol system according to claim 1, which is characterized in that the waterworks further include water storage device,
The water inlet end of the water storage device is connected to the cold water source and thermal water source, and water outlet is connected to described by the first liquid pumping device
Emulsification pretreatment device.
3. continuous colloidal sol system according to claim 2, which is characterized in that first liquid pumping device is electrically connected at institute
Flow measurement device is stated, the flow measurement device adjusts the work of first liquid pumping device according to preset pump liquid flow value
State.
4. continuous colloidal sol system according to claim 1, which is characterized in that the blanking device further includes for containing glue
The feed bin of powder, the discharge end of the feed bin are connected to the discharge, are additionally provided with feeding port on the feed bin.
5. continuous colloidal sol system according to claim 4, which is characterized in that it is additionally provided with exhaust blower on the blanking device,
The air intake and feeding port of the exhaust blower are disposed adjacent.
6. continuous colloidal sol system according to claim 1, which is characterized in that between the discharge and emulsification pretreatment device
Equipped with baiting valve, the baiting valve is opened when the waterworks reach a preset pump liquid flow value and discharges rubber powder.
7. continuous colloidal sol system according to claim 1, which is characterized in that there is agitating device on the storage device,
The agitating device includes stirring driver and being connected to the stirring driver and the mixing part of glue is protruded into one end.
8. continuous colloidal sol system according to claim 1, which is characterized in that the emulsification pretreatment device be connected to it is described to
The feed end of water installations is equipped with the first valve, and the discharge end of the emulsification pretreatment device is equipped with the second valve.
9. continuous colloidal sol system according to claim 1, which is characterized in that the emulsification pretreatment device and storage device it
Between be equipped with the second liquid pumping device.
10. continuous colloidal sol system according to claim 1, which is characterized in that the bottom of the storage device is funnel-shaped
Structure and there is the blow-off valve that communicates therewith.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821544075.6U CN208927950U (en) | 2018-09-20 | 2018-09-20 | Continuous colloidal sol system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821544075.6U CN208927950U (en) | 2018-09-20 | 2018-09-20 | Continuous colloidal sol system |
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| Publication Number | Publication Date |
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| CN208927950U true CN208927950U (en) | 2019-06-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201821544075.6U Active CN208927950U (en) | 2018-09-20 | 2018-09-20 | Continuous colloidal sol system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109200838A (en) * | 2018-09-20 | 2019-01-15 | 佛山市海天（江苏）调味食品有限公司 | Continuous colloidal sol system |
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2018
- 2018-09-20 CN CN201821544075.6U patent/CN208927950U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109200838A (en) * | 2018-09-20 | 2019-01-15 | 佛山市海天（江苏）调味食品有限公司 | Continuous colloidal sol system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210513 Address after: 223800 No. 889 Suzhou Road, Suqian Economic and Technological Development Zone, Sucheng District, Suqian City, Jiangsu Province Patentee after: Haitian oyster sauce (Jiangsu) Food Co.,Ltd. Patentee after: FOSHAN HAITIAN (JIANGSU) FLAVOURING FOOD Co.,Ltd. Patentee after: FOSHAN HAITIAN FLAVORING & FOOD Co.,Ltd. Address before: 223800 no.889 Suzhou Road, Suqian Economic and Technological Development Zone, Jiangsu Province Patentee before: FOSHAN HAITIAN (JIANGSU) FLAVOURING FOOD Co.,Ltd. Patentee before: FOSHAN HAITIAN FLAVORING & FOOD Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 223800 No. 889 Suzhou Road, Suqian Economic and Technological Development Zone, Sucheng District, Suqian City, Jiangsu Province Patentee after: Haitian oyster sauce (Jiangsu) Food Co.,Ltd. Patentee after: Haitian vinegar Group Co.,Ltd. Patentee after: FOSHAN HAITIAN FLAVORING & FOOD Co.,Ltd. Address before: 223800 No. 889 Suzhou Road, Suqian Economic and Technological Development Zone, Sucheng District, Suqian City, Jiangsu Province Patentee before: Haitian oyster sauce (Jiangsu) Food Co.,Ltd. Patentee before: FOSHAN HAITIAN (JIANGSU) FLAVOURING FOOD Co.,Ltd. Patentee before: FOSHAN HAITIAN FLAVORING & FOOD Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220119 Address after: 223800 Zone E, No. 889, Suzhou Road, Suqian Economic and Technological Development Zone, Suqian City, Jiangsu Province Patentee after: Foshan Haitian (Suqian) seasoning Food Co.,Ltd. Patentee after: Haitian oyster sauce (Tianjin) Group Co.,Ltd. Patentee after: FOSHAN HAITIAN FLAVORING & FOOD Co.,Ltd. Address before: 223800 No. 889 Suzhou Road, Suqian Economic and Technological Development Zone, Sucheng District, Suqian City, Jiangsu Province Patentee before: Haitian oyster sauce (Jiangsu) Food Co.,Ltd. Patentee before: Haitian vinegar Group Co.,Ltd. Patentee before: FOSHAN HAITIAN FLAVORING & FOOD Co.,Ltd. |
|
| TR01 | Transfer of patent right |