CN108939961A - Continuous colloidal sol equipment - Google Patents
Continuous colloidal sol equipment Download PDFInfo
- Publication number
- CN108939961A CN108939961A CN201811105367.4A CN201811105367A CN108939961A CN 108939961 A CN108939961 A CN 108939961A CN 201811105367 A CN201811105367 A CN 201811105367A CN 108939961 A CN108939961 A CN 108939961A
- Authority
- CN
- China
- Prior art keywords
- colloidal sol
- emulsification pretreatment
- waterworks
- valve
- pretreatment device
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 50
- 238000004945 emulsification Methods 0.000 claims abstract description 43
- 239000000843 powder Substances 0.000 claims abstract description 30
- 238000003860 storage Methods 0.000 claims abstract description 26
- 239000003292 glue Substances 0.000 claims abstract description 22
- 238000000034 method Methods 0.000 claims abstract description 18
- 238000005259 measurement Methods 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 238000009434 installation Methods 0.000 claims description 3
- 238000004090 dissolution Methods 0.000 abstract description 8
- 235000013305 food Nutrition 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 4
- 238000010008 shearing Methods 0.000 description 4
- 229920001285 xanthan gum Polymers 0.000 description 3
- 239000000230 xanthan gum Substances 0.000 description 3
- 229940082509 xanthan gum Drugs 0.000 description 3
- 235000010493 xanthan gum Nutrition 0.000 description 3
- 239000006071 cream Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000003995 emulsifying agent Substances 0.000 description 2
- 239000000693 micelle Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 108010010803 Gelatin Proteins 0.000 description 1
- 206010054949 Metaplasia Diseases 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000015689 metaplastic ossification Effects 0.000 description 1
- 238000011897 real-time detection Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F21/00—Dissolving
- B01F21/30—Workflow diagrams or layout of plants, e.g. flow charts; Details of workflow diagrams or layout of plants, e.g. controlling means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F21/00—Dissolving
- B01F21/10—Dissolving using driven stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
- B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/21—Measuring
- B01F35/211—Measuring of the operational parameters
- B01F35/2111—Flow rate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/21—Measuring
- B01F35/211—Measuring of the operational parameters
- B01F35/2112—Level of material in a container or the position or shape of the upper surface of the material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/22—Control or regulation
- B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
- B01F35/2214—Speed during the operation
- B01F35/22141—Speed of feeding of at least one component to be mixed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/716—Feed mechanisms characterised by the relative arrangement of the containers for feeding or mixing the components
- B01F35/7163—Feed mechanisms characterised by the relative arrangement of the containers for feeding or mixing the components the containers being connected in a mouth-to-mouth, end-to-end disposition, i.e. the openings are juxtaposed before contacting the contents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/06—Mixing of food ingredients
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The present invention relates to colloidal sol fields, relate to a kind of continuous colloidal sol equipment, two feed ends of its emulsification pretreatment device are connected to waterworks and blanking device, waterworks are for providing the process water of proper temperature, and it can detect that the flow of process water by flow measurement device, blanking device then controls the blanking velocity of rubber powder by discharge, process water and rubber powder are mixed and are sheared uniformly by emulsification pretreatment device, rubber powder is realized quickly with this and continuous-dissolution is to form glue, glue is flowed in storage tank from the discharge end of emulsification pretreatment device and is stored, in case food processing uses.
Description
Technical field
The present invention relates to colloidal sol fields, more particularly to a kind of continuous colloidal sol equipment.
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.
Summary of the invention
To solve the above-mentioned problems, it the object of the present invention is to provide a kind of continuous colloidal sol equipment, is set with solving existing colloidal sol
It is standby can not high-volume continuous-dissolution rubber powder the problem of.
Based on this, the present invention provides a kind of continuous colloidal sol equipment, including waterworks, blanking device, emulsification pretreatment to fill
It sets and storage tank, the waterworks and blanking device are connected to two feed ends of the emulsification pretreatment device, described
The discharge end of emulsification pretreatment device is connected to the storage tank；It is equipped between the waterworks and emulsification pretreatment device for examining
Survey the flow measurement device of the feedwater flow of waterworks, the blanking device includes feed bin for containing rubber powder and is located at institute
State the discharge discharge end of feed bin and for controlling rubber powder blanking velocity.
Preferably, the waterworks include the hot water valve for being connected to thermal water source and the cold water for being connected to cold water source
Valve, the hot water valve and cold valves are arranged in parallel, and the cold water mix shape of the hot water of hot water valve discharge and cold valves discharge
At 45~55 DEG C of process water.
Preferably, the feed bin structure funnel-shaped, the top of the feed bin has feeding port.
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 feedwater flow and discharge rubber powder.
Preferably, having the agitating device and liquid level sensing device for stirring glue, institute in the storage tank
It states agitating device and is electrically connected at the liquid level sensing device.
Preferably, the bottom of storage tank structure funnel-shaped, the bottom of the storage tank are connected to blow-off valve.
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 discharging pump between the emulsification pretreatment device and storage tank.
Continuous colloidal sol equipment of the invention, two feed ends of emulsification pretreatment device are connected to waterworks under
Expect that device, waterworks can detect that the stream of process water by flow measurement device for providing the process water of proper temperature
Amount, blanking device then control the blanking velocity of rubber powder by discharge, and process water and rubber powder are mixed and cut by emulsification pretreatment device
It cuts uniformly, rubber powder is realized quickly with this and continuous-dissolution is to form glue, glue is flowed to from the discharge end of emulsification pretreatment device
It is stored in storage tank, in case food processing uses.
Detailed description of the invention
Fig. 1 is the overall structure diagram of the continuous colloidal sol equipment of the embodiment of the present invention；
Fig. 2 is the structural schematic diagram of the waterworks of the continuous colloidal sol equipment of the embodiment of the present invention；
Fig. 3 is the structural schematic diagram of the blanking device of the continuous colloidal sol equipment of the embodiment of the present invention；
Fig. 4 is the structural schematic diagram of the storage tank of the continuous colloidal sol equipment of the embodiment of the present invention.
Wherein, 1, waterworks；11, cold water source；12, thermal water source；13, cold valves；14, hot water valve；2, blanking device；
21, discharge；22, feed bin；221, feeding port；23, exhaust blower；24, baiting valve；3, emulsification pretreatment device；31, the first valve；
32, the second valve；4, storage tank；41, agitating device；42, discharging pump；43, blow-off valve；5, flow measurement device.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiments of the present invention will be described in further detail.Implement below
Example is not intended to limit the scope of the invention for illustrating the present invention.
In connection with Figures 1 to 4, schematically showing continuous colloidal sol equipment of the invention, including waterworks 1, blanking
Device 2, emulsification pretreatment device 3 and storage tank 4, wherein emulsification pretreatment device 3 is preferably high speed shear pump.Waterworks 1 are under
Material device 2 is connected to two feed ends of emulsification pretreatment device 3, and specifically, emulsification pretreatment device 3 has liquid feedstock end
With feeding-in solid body end, waterworks 1 are connected to the liquid feedstock end of emulsification pretreatment device 3, and blanking device 2 is connected to shearing cream
3 solid liquid feeding end is set in makeup.The discharge end of emulsification pretreatment device 3 is for being discharged solidliquid mixture, and the discharge end is connected to
Storage tank 4.In conjunction with shown in Fig. 2 and Fig. 3, in order to control the mixed proportion of water and rubber powder in glue, waterworks 1 and shearing cream
The flow measurement device 5 being equipped between 3 for detecting the feedwater flow of waterworks 1 is set in makeup, and blanking device 2 includes material
Storehouse 22 and discharge 21 can keep in rubber powder in feed bin 22 and provide rubber powder to discharge 21, and discharge 21 is connected to feed bin 22
Discharge end and the blanking velocity for controlling rubber powder blanking to emulsification pretreatment device 3, it is preferred that discharge 21 is rotary valve.Continuous
When mass production, waterworks 1 provide the process water of proper temperature, and the inflow of 5 real-time detection process water of flow measurement device is cut
Cut the flow of emulsifier unit 3, blanking device 2 controls the blanking velocity of rubber powder by discharge 21, and emulsification pretreatment device 3 is by technique
Water and rubber powder are mixed and are sheared uniformly, realize rubber powder quickly and continuous-dissolution is to form glue, final glue is filled from emulsification pretreatment
The discharge end for setting 3 is discharged into storage tank 4, in case food processing uses.
Specifically, waterworks 1 are including being connected to the hot water valve 14 of thermal water source 12 and being connected to the cold water of cold water source 11
Valve 13, hot water valve 14 and cold valves 13 are arranged in parallel, the hot water and cold water that hot water and cold water mix, hot water valve 14 are discharged
The cold water mix that valve 13 is discharged forms 45~55 DEG C of process water, and process water water temperature is preferably 55 DEG C.The knot funnel-shaped of feed bin 22
Structure, discharge end is connected to discharge 21, and the top of feed bin 22 also has feeding port 221, throwing of the staff from feed bin 22
Material mouth 221 puts into rubber powder, and rubber powder is fallen into discharge 21 from the discharge end of 22 bottom of feed bin under gravity, to prevent glue
The dust recycling that generates when powder is launched is additionally provided with exhaust blower 23 on blanking device 2, the air intake and feeding port of the exhaust blower 23
221 are disposed adjacent, to adsorb the dust near feeding port 221.Baiting valve is equipped between discharge 21 and emulsification pretreatment device 3
24, after the process water that waterworks 1 provide reaches preset pump liquid flow value, baiting valve 24 is opened and is discharged into rubber powder and cuts
It cuts in emulsifier unit 3.
As shown in connection with fig. 4, there is agitating device 41 and liquid level sensing device (not shown), agitating device in storage tank 4
41 include stirring driver and are connected to stirring driver and the mixing part of glue is protruded into one end, and mixing part is in stirring driver
Driving under futher stir dispersion glue, it is uneven to prevent local gelatin concentration or caking phenomenon occur.41 electricity of agitating device
Property be connected to liquid level sensing device, when the glue liquid level in storage tank 4 reaches a certain default liquid level, agitating device 41 start simultaneously
Stir glue.In order to be discharged the glue in storage device for food processing use, the bottom of storage device knot funnel-shaped
Structure and there is the blow-off valve 43 that communicates therewith, opening blow-off valve 43, the glue in storage device can be discharged.
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, in disassembly, cleaning or maintenance emulsification pretreatment device 3, closes baiting valve 24, first
Emulsification pretreatment device 3 can be cut off removing by valve 31 and the second valve 32 from the system.Emulsification pretreatment device 3 and storing
Discharging pump 42 is additionally provided between device, the glue that emulsification pretreatment device 3 is discharged can be actively pumped to storage device by discharging pump 42
In, so that the mixing shearing work of emulsification pretreatment device 3 is more smooth.
In conclusion continuous colloidal sol equipment of the invention, two feed ends of emulsification pretreatment device 3 be connected to
Water installations 1 and blanking device 2, waterworks 1 can be examined for providing the process water of proper temperature, and by flow measurement device 5
Measure the flow of process water, blanking device 2 then controls the blanking velocity of rubber powder by discharge 21, and emulsification pretreatment device 3 is by work
Skill water and rubber powder are mixed and are sheared uniformly, realize rubber powder quickly with this and continuous-dissolution is to form glue, and glue is from emulsification pretreatment
The discharge end of device 3 is flowed in storage tank 4 and is stored, in case food processing uses.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For member, without departing from the technical principles of the invention, several improvement and replacement can also be made, these are improved and replacement
Also it should be regarded as protection scope of the present invention.
Claims (9)
1. a kind of continuous colloidal sol equipment, which is characterized in that including waterworks, blanking device, emulsification pretreatment device and storage tank,
The waterworks and blanking device are connected to two feed ends of the emulsification pretreatment device, the emulsification pretreatment device
Discharge end be connected to the storage tank；It is equipped between the waterworks and emulsification pretreatment device for detecting waterworks
The flow measurement device of feedwater flow, the blanking device include the feed bin for containing rubber powder and the discharging positioned at the feed bin
Discharge holding and for controlling rubber powder blanking velocity.
2. continuous colloidal sol equipment according to claim 1, which is characterized in that the waterworks include being connected to thermal water source
Hot water valve and be connected to the cold valves of cold water source, the hot water valve and cold valves are arranged in parallel, and the hot water valve is discharged
Hot water and the cold water mix of cold valves discharge form 45~55 DEG C of process water.
3. continuous colloidal sol equipment according to claim 1, which is characterized in that the feed bin structure funnel-shaped, the material
The top in storehouse has feeding port.
4. continuous colloidal sol equipment according to claim 3, 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.
5. continuous colloidal sol equipment 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 feedwater flow and discharges rubber powder.
6. continuous colloidal sol equipment according to claim 1, which is characterized in that have in the storage tank for stirring glue
Agitating device and liquid level sensing device, the agitating device is electrically connected at the liquid level sensing device.
7. continuous colloidal sol equipment according to claim 1, which is characterized in that the bottom of storage tank knot funnel-shaped
The bottom of structure, the storage tank is connected to blow-off valve.
8. continuous colloidal sol equipment 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 equipment according to claim 1, which is characterized in that between the emulsification pretreatment device and storage tank
Equipped with discharging pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811105367.4A CN108939961A (en) | 2018-09-20 | 2018-09-20 | Continuous colloidal sol equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811105367.4A CN108939961A (en) | 2018-09-20 | 2018-09-20 | Continuous colloidal sol equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108939961A true CN108939961A (en) | 2018-12-07 |
Family
ID=64472020
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811105367.4A Pending CN108939961A (en) | 2018-09-20 | 2018-09-20 | Continuous colloidal sol equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108939961A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110327852A (en) * | 2019-07-06 | 2019-10-15 | 江西奕方农业科技有限公司 | Colloidal sol equipment and its manufacturing method |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101395207A (en) * | 2006-12-21 | 2009-03-25 | 克莱顿聚合物研究有限公司 | Process for the preparation of an artificial latex |
| CN207786362U (en) * | 2018-01-10 | 2018-08-31 | 玖龙纸业（太仓）有限公司 | A kind of on-line dilution emulsifier unit of liquid particulate retention agent |
| CN208927951U (en) * | 2018-09-20 | 2019-06-04 | 佛山市海天（江苏）调味食品有限公司 | Continuous colloidal sol equipment |
-
2018
- 2018-09-20 CN CN201811105367.4A patent/CN108939961A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101395207A (en) * | 2006-12-21 | 2009-03-25 | 克莱顿聚合物研究有限公司 | Process for the preparation of an artificial latex |
| CN207786362U (en) * | 2018-01-10 | 2018-08-31 | 玖龙纸业（太仓）有限公司 | A kind of on-line dilution emulsifier unit of liquid particulate retention agent |
| CN208927951U (en) * | 2018-09-20 | 2019-06-04 | 佛山市海天（江苏）调味食品有限公司 | Continuous colloidal sol equipment |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110327852A (en) * | 2019-07-06 | 2019-10-15 | 江西奕方农业科技有限公司 | Colloidal sol equipment and its manufacturing method |
| CN110327852B (en) * | 2019-07-06 | 2022-07-12 | 江西奕方农业科技有限公司 | Sol device and method for manufacturing the same |
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|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181207 |
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| RJ01 | Rejection of invention patent application after publication |