CN109908778A - A kind of device and method of continuous production emulsion - Google Patents
A kind of device and method of continuous production emulsion Download PDFInfo
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- CN109908778A CN109908778A CN201910201571.4A CN201910201571A CN109908778A CN 109908778 A CN109908778 A CN 109908778A CN 201910201571 A CN201910201571 A CN 201910201571A CN 109908778 A CN109908778 A CN 109908778A
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- 239000007788 liquid Substances 0.000 claims abstract description 40
- 238000004945 emulsification Methods 0.000 claims abstract description 38
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 35
- 239000002270 dispersing agent Substances 0.000 claims abstract description 32
- 238000004519 manufacturing process Methods 0.000 claims abstract description 20
- 230000008676 import Effects 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 55
- 239000006185 dispersion Substances 0.000 claims description 38
- 239000012188 paraffin wax Substances 0.000 claims description 21
- 239000012530 fluid Substances 0.000 claims description 14
- 229920001732 Lignosulfonate Polymers 0.000 claims description 8
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- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 6
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- 239000011344 liquid material Substances 0.000 claims description 2
- 238000002844 melting Methods 0.000 claims description 2
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- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 description 6
- 239000002023 wood Substances 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000010992 reflux Methods 0.000 description 3
- 238000004078 waterproofing Methods 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000006071 cream Substances 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
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- 229920002522 Wood fibre Polymers 0.000 description 1
- 229920005551 calcium lignosulfonate Polymers 0.000 description 1
- RYAGRZNBULDMBW-UHFFFAOYSA-L calcium;3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfonatopropyl)phenoxy]propane-1-sulfonate Chemical compound [Ca+2].COC1=CC=CC(CC(CS([O-])(=O)=O)OC=2C(=CC(CCCS([O-])(=O)=O)=CC=2)OC)=C1O RYAGRZNBULDMBW-UHFFFAOYSA-L 0.000 description 1
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- YDEXUEFDPVHGHE-GGMCWBHBSA-L disodium;(2r)-3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfonatopropyl)phenoxy]propane-1-sulfonate Chemical compound [Na+].[Na+].COC1=CC=CC(C[C@H](CS([O-])(=O)=O)OC=2C(=CC(CCCS([O-])(=O)=O)=CC=2)OC)=C1O YDEXUEFDPVHGHE-GGMCWBHBSA-L 0.000 description 1
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- Colloid Chemistry (AREA)
Abstract
The present invention discloses a kind of device and method of continuous production emulsion, is related to emulsion production technical field, and device includes liquid feed device, head tank, emulsification, dispersal device, intermediate buffer tank and output pipe；The liquid feed device is for providing a variety of different emulsifiers or aqueous dispersant, the head tank is for storing raw material to be emulsified, the liquid feed device is connected with liquid feeding pipeline, the head tank is connected with raw material pipeline, and the raw material pipeline and the liquid feeding pipeline are connect with the input terminal of the emulsification, dispersal device；The emulsification, dispersal device output end connect with the import of the intermediate buffer tank by connecting line, the outlet connection output pipe of the intermediate buffer tank.The device of the invention can be erected at client production scene, be conducive to control product quality, and can according to need the formula and partial size of selection emulsion, meet a variety of work requirements.
Description
Technical field
The present invention relates to emulsion production technical fields, device and side more particularly to a kind of continuous production emulsion
Method.
Background technique
Emulsion refers to that the disperse system as composed by two kinds of immiscible liquid, i.e., a kind of liquid are divided in the form of droplet
It is dispersed in the mixture formed among another liquid.Now, emulsion in the industrial production using more and more extensive, such as
Paraffin emulsion can be used as waterproofing agent, be widely used in the waterproof of wood-based plate.
Currently, emulsion is when in use, usually after the completion of emulsion production, it is cooled down, then will
Packaged emulsion transports client production scene, carries out subsequent use, and packaging and transportation cost are higher.And it is existing
Required plurality of raw materials is usually mixed in a storage tank, then passes through physics by some emulsion production equipments
Mixing dispersion forms emulsion, and emulsion type produced is single, and the proportion of various raw materials is unable to get effective tune
It is whole；Moreover, after the completion of emulsions, or when entire production equipment is shut down suddenly, can not have to entire pipeline
Effect cleaning；Existing production equipment can not also adjust the dispersion particle diameter of emulsion well.
Summary of the invention
The object of the present invention is to provide a kind of device and methods of continuous production emulsion, to solve present in the prior art
The above problem, device can be erected at client production scene, be conducive to control product quality, and can according to need selection cream
The formula and partial size of turbid, meet a variety of work requirements, also achieve the automatic cleaning of equipment.
To achieve the above object, the present invention provides following schemes: the present invention provides a kind of dress of continuous production emulsion
It sets, including liquid feed device, head tank, emulsification, dispersal device, intermediate buffer tank and output pipe；The liquid feed device is for mentioning
For the emulsifier or aqueous dispersant of a variety of different formulations, the head tank is for storing raw material to be emulsified, the feed flow dress
Set and be connected with liquid feeding pipeline, the head tank is connected with raw material pipeline, the raw material pipeline and the liquid feeding pipeline with it is described
Emulsification, the input terminal connection of dispersal device；The emulsification, dispersal device output end pass through connecting line and the intermediate buffer
The import of tank connects, and the outlet of the intermediate buffer tank connects the output pipe.
Preferably, the liquid feed device includes dispersion tank and multiple original fluid containers, is respectively provided with not in each original fluid container
Congener emulsifier or dispersing agent；The original fluid container by control valve, flowmeter and metering pump and the dispersion tank into
The outlet of mouth connection, the dispersion tank connects the liquid feeding pipeline；The top of the dispersion tank is additionally provided with hot water inlet connection
Hot-water cylinder, for providing hot water.
Preferably, control valve, flowmeter, filter and metering pump are disposed on the raw material pipeline；The feed flow
Control valve, flowmeter, filter and metering pump are disposed on pipeline.
Preferably, the outlet of the head tank, dispersion tank and intermediate buffer tank is also respectively connected with blow-off valve, the mother tube
Road and the liquid feeding pipeline are again provided with blow-off valve close to the side of the emulsification, dispersal device.
Preferably, the hot-water cylinder is connected with hot water main pipe, and the hot water main pipe is equipped with control valve, flowmeter and metering
Pump；The hot water main pipe is also connected with two-way hot-water branch, connect all the way with the hot water inlet of the dispersion tank, another way and institute
State the control valve connection being arranged on raw material pipeline；The connecting line is connected with two-way by control valve and connects branch, all the way institute
It states connection branch to connect with the import of the intermediate buffer tank, another way and the output pipe are close to the intermediate buffer tank
One end connection；The output pipe is provided with control valve, flowmeter and metering pump, and the output pipe is additionally provided with circuit and institute
State intermediate buffer tank, hot-water cylinder connection.
Preferably, it is described emulsification, dispersal device be provided with it is multiple；The emulsification, dispersal device use mulser, homogenizer
Or Homogenizing pump；It is described to emulsify, be provided with glass peephole on the connecting line of the output end of dispersal device connection.
Preferably, the raw material to be emulsified includes paraffin, the emulsifier or dispersion of the emulsifier or aqueous dispersant
Agent includes lignosulfonates and/or polyvinyl alcohol, by weight, 40~60 parts of paraffin, emulsifier or 1~5 part of dispersing agent,
40~60 parts of water.
Preferably, the device of the continuous production emulsion is set in a set casing body.
A kind of method of continuous production emulsion is also disclosed in the present invention, comprising the following steps:
1) by raw material heating and melting to be emulsified at liquid, and raw material liq to be emulsified is pumped by head tank by feeding pump
In；
2) water in hot-water cylinder is heated to 80-90 DEG C, and be added in dispersion tank；
3) as needed, select emulsifier or dispersing agent, and by specified original fluid container emulsifier or dispersing agent according to than
Example is added in dispersion tank, and is dissolved into hot water, and emulsifier or aqueous dispersant are formed；
4) according to the partial size of emulsion finished product and cut mode selection emulsification, dispersal device, and by raw material pipeline and
The emulsification of liquid feeding pipeline and selection, dispersal device connection；
5) liquid raw material to be emulsified and emulsifier or aqueous dispersant are extracted by predetermined ratio, and passes through emulsification, dispersion
Device, which carries out physical mixed dispersion, becomes emulsion；
6) emulsion processed is pumped into intermediate buffer tank；
7) emulsion in intermediate buffer tank is delivered to by subsequent production line by output pipe.
Preferably, in the step 1), raw material to be emulsified is paraffin, and heating temperature is 80-90 DEG C；It is newborn in the step 3)
Agent or dispersing agent are lignosulfonates and/or polyvinyl alcohol.
The present invention achieves following technical effect compared with the existing technology:
1) device of continuous production emulsion of the present invention can be erected at client production scene, and field fabrication, scene uses, and have
Product quality is controlled conducive to client, and whole device is controlled by full-automatic PLC, saved artificial；
2) multiple original fluid containers and head tank are provided with, can according to need provide a variety of different emulsifiers or dispersing agent and
Raw material to be emulsified is added raw material by different formulas to realize, processes a variety of different emulsion；And pass through the control of setting
Valve processed, metering pump, flowmeter etc. can control the ratio of various raw materials；
3) a variety of different types of emulsifications, dispersal device are set, can according to need selection emulsion cut mode or
Person's partial size meets a variety of needs of work；
4) the automatic cleaning of pipeline and equipment is realized, and ejected wash water realization recycles, zero-emission, energy conservation and environmental protection.
Detailed description of the invention
It in order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, below will be to institute in embodiment
Attached drawing to be used is needed to be briefly described, it should be apparent that, the accompanying drawings in the following description is only some implementations of the invention
Example, for those of ordinary skill in the art, without creative efforts, can also obtain according to these attached drawings
Obtain other attached drawings.
Fig. 1 is the structural schematic diagram of the device of continuous production emulsion in the present invention；
1, head tank, 2, dispersion tank, 3, original fluid container, 4, emulsification, dispersal device, 5, intermediate buffer tank, 6, hot-water cylinder, 7, meter
Amount pump, 8, control valve, 9, flowmeter, 10, filter, 11, glass peephole, 12, feeding pump, 13, blow-off valve.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
The object of the present invention is to provide a kind of device and methods of continuous production emulsion, to solve present in the prior art
The above problem, device can be erected at client production scene, be conducive to control product quality, and can according to need selection cream
The formula and partial size of turbid, meet a variety of work requirements, also achieve the automatic cleaning of equipment.
In order to make the foregoing objectives, features and advantages of the present invention clearer and more comprehensible, with reference to the accompanying drawing and specific real
Applying mode, the present invention is described in further detail.
Embodiment one
As shown in Figure 1, the present embodiment provides a kind of device of continuous production emulsion, including liquid feed device, head tank 1,
Emulsification, dispersal device 4, intermediate buffer tank 5 and output pipe；The liquid feed device is for providing a variety of different emulsifiers or dividing
Powder aqueous solution, for the head tank 1 for storing raw material to be emulsified, the liquid feed device is connected with liquid feeding pipeline, the raw material
Tank 1 is connected with raw material pipeline, and the input terminal of the raw material pipeline and the liquid feeding pipeline with the emulsification, dispersal device 4 connects
It connects；The emulsification, dispersal device 4 output end connect with the import of the intermediate buffer tank 5 by connecting line, the centre
The outlet of buffer tank 5 connects the output pipe, and output pipe is attached with subsequent production line.The continuous life of the present embodiment
The device of galactopoiesis turbid can be erected at client production scene, and field fabrication, scene uses, and be conducive to client and control product quality,
And whole device is controlled by full-automatic PLC, is saved artificial.
In the present embodiment, the liquid feed device includes dispersion tank 2 and multiple original fluid containers 3, is divided in each original fluid container 3
It Zhuan You not different types of emulsifier or dispersing agent；The original fluid container 3 by control valve 8, flowmeter 9 and metering pump 7 with it is described
The import of dispersion tank 2 connects, and the outlet of the dispersion tank 2 connects the liquid feeding pipeline；The top of the dispersion tank 2 is additionally provided with
Hot water inlet connects hot-water cylinder 6, for providing hot water；And head tank 1 also can be set it is multiple, it is different to be emulsified to provide
Raw material.
Further, control valve 8, flowmeter 9, filter 10 and metering pump 7 are disposed on the raw material pipeline；Institute
It states and is disposed with control valve 8, flowmeter 9, filter 10 and metering pump 7 on liquid feeding pipeline, filter 10 uses existing mistake
Filter is filtered for treating emulsified feedstock solution and emulsifier or aqueous dispersant；The hot-water cylinder 6 is connected with
Hot water main pipe, for connecting with dispersion tank 2, the hot water main pipe is equipped with control valve 8, flowmeter 9 and metering pump 7.
It is provided with multiple original fluid containers 3 and head tank 1 in the present embodiment, a variety of different emulsifiers or dispersing agent can be provided
With raw material to be emulsified, raw material is added by different formulas to realize, processes a variety of different emulsion；And pass through setting
Control valve 8, metering pump 7, flowmeter 9 etc. can control the ratio of various raw materials.
The outlet of the head tank 1, dispersion tank 2 and intermediate buffer tank 5 is also respectively connected with blow-off valve 13, the raw material pipeline
Blow-off valve 13 is again provided with close to the side of the emulsification, dispersal device 4 with the liquid feeding pipeline；Be arranged blow-off valve 13 so as to
After the completion of work, various raw materials are discharged from blow-off valve, are recycled.
In the present embodiment, raw material to be emulsified preferentially selects paraffin, the emulsifier of the emulsifier or aqueous dispersant
Or dispersing agent includes that lignosulfonates and/or polyvinyl alcohol include by weight in paraffin wax emulsion after processing is completed
40~60 parts of paraffin, emulsifier or 1~5 part of dispersing agent, 40~60 parts of water；The paraffin wax emulsion is applied to artificial as waterproofing agent
In plate, the production line of output pipe connection is existing artificial board product line.In the present embodiment, the lignosulfonates can
To increase the dispersibility and mobility of emulsion, reduce the dynamics of paraffin molecule, dilution dispersion paraffin reduces the use of paraffin
Amount, lignosulfonates use sodium lignin sulfonate or calcium lignosulfonate；The polyvinyl alcohol effectively can disperse and increase
Add dispersion suspension time, suspension effect and the colloid protecting effect of paraffin in water, meanwhile, there is bonding toughening to wood fibre
Effect.
In the present embodiment, the emulsification, dispersal device 4 are provided with multiple and different types；The emulsification, dispersal device
4 using mulser, homogenizer or Homogenizing pump, and specifically, mulser can select vertical homogeneous head, planetary stirring machine, bottom
Formula homogeneous head etc.；Homogenizer can select ordinary high pressure homogenizer or pneumatic control high pressure homogenizer etc.；Homogenizing pump can be selected
Three-level pipeline emulsification pump, single-stage emulsification pump etc..It is described to emulsify, on the connecting line of the output end of dispersal device 4 connection
It is provided with transparent glass peephole 11, the paraffin wax emulsion after facilitating observation to process.
A variety of different types of emulsifications, dispersal device are set in the present embodiment, can according to need cutting for selection emulsion
Butt formula or partial size (preferably nanoscale or micron order), meet a variety of needs of work.
In the present embodiment, the hot water main pipe is also connected with two-way hot-water branch, all the way with the hot water of the dispersion tank 2
Import connection, for forming emulsifier or aqueous dispersant with emulsifier or dispersant in dispersion tank, another way with
The control valve 8 being arranged on the raw material pipeline connects, for providing hot water detergent line.
The connecting line is connected with two-way by control valve 8 and connects branch, all the way the connection branch and the centre
The import of buffer tank 5 connects, and another way is connect with the output pipe close to one end of the intermediate buffer tank 5；The output
Piping connection has two reflux branches, and one end of a reflux branch is connected on the output pipe after metering pump 7
Side, the other end are connect with the intermediate buffer tank 5；One end of another reflux branch is connected to going out for the output pipe
Mouthful, the other end connects the intermediate buffer tank 5 and hot-water cylinder 6；The output pipe is provided with control valve 8, flowmeter 9 and metering
Pump 7, in order to input quantitative emulsion into subsequent production line.
After the completion of work, pipeline can be cleaned by the hot water in hot-water cylinder 6, and ejected wash water realizes circulation
It utilizes, zero-emission, energy conservation and environmental protection.
In the present embodiment, the device of the continuous production emulsion is set in a set casing body, and realization is entirely set
Standby over all Integration, it is compact-sized.
In the present embodiment, a kind of method of continuous production emulsion (paraffin wax emulsion) is also disclosed, comprising the following steps:
1) paraffin that paraffin is put into workshop is melted in slot, is heated to 80-90 DEG C and is melted into liquid, and passes through feeding pump
12 are pumped into liquid in head tank 1；
2) water in hot-water cylinder 6 is heated to 80-90 DEG C, and be added in dispersion tank 2；
3) emulsifier or dispersing agent-lignosulfonates and/or polyvinyl alcohol as needed, are selected, and by specified stoste
Emulsifier or dispersing agent in tank 3 are added in dispersion tank 2 according to ratio, and are dissolved into hot water, and emulsifier or dispersion are formed
Agent aqueous solution；
4) according to the partial size of emulsion finished product and cut mode selection emulsification, dispersal device 4, and by raw material pipeline and
The emulsification of liquid feeding pipeline and selection, dispersal device 4 connect；
5) liquid paraffin and emulsifier or aqueous dispersant are extracted by predetermined ratio, and by emulsification, dispersal device 4 into
The dispersion of row physical mixed becomes emulsion；
6) emulsion processed is pumped into intermediate buffer tank 5；
7) subsequent Wood-based Panel Production is delivered to for the emulsion in intermediate buffer tank 5 as waterproofing agent by output pipe
Line；
8) it is in defibrator discharging spiral shell that the application position of artificial board product line, which includes: medium/high density fiber board application position,
Revolve the position of (as the application position of melt paraffin) or the shotcrete pipe that discharges；The application position of particieboard is in sandwich layer and surface layer
Wood shavings are into below blanking belt before glue mixer；The application position of oriented wood chipboard be surface layer wood shavings and long state sandwich layer wood shavings into
Position before glue mixer.
Wherein, each pipeline is steam tracing in the present embodiment.
After the completion of work or after equipment is shut down suddenly, because can be coagulated after raw material to be emulsified (such as atoleine) is cooling
Gu, it is therefore desirable to the raw material in pipeline is discharged by recycling by blow-off valve 13, wherein the liquid paraffin in such as raw material pipeline can
Melted in slot with being recycled to the paraffin of head tank 1 or workshop, the emulsion finished product in output pipe can be back to centre
In buffer tank 5.After the completion of discharge, also pipeline is cleaned；Hot water enters original by hot water branch first in hot-water cylinder
It is cleaned in expects pipe road, then in turn through emulsification, dispersal device, connecting line, connecting branch, output pipe, to whole
A pipeline is cleaned, and water for cleaning can be expelled directly out, and also be can according to need the branch that flowed back and is back to intermediate buffer tank 5
Or be recycled in hot-water cylinder 6, reduce waste.
Wherein, because will not be solidified after emulsifier or aqueous dispersant are cooling, not necessarily to liquid feeding pipeline
It is cleaned；Hot water branch can certainly be added to be attached with liquid feeding pipeline, it is equally rinsed, improve and rinse effect
Fruit.
Specific examples are applied in the present invention, and principle and implementation of the present invention are described, above embodiments
Illustrate to be merely used to help understand method and its core concept of the invention；At the same time, for those skilled in the art, according to
According to thought of the invention, there will be changes in the specific implementation manner and application range.In conclusion the content of the present specification
It should not be construed as limiting the invention.
Claims (10)
1. a kind of device of continuous production emulsion, it is characterised in that: including liquid feed device, head tank, emulsification, dispersal device,
Intermediate buffer tank and output pipe；The liquid feed device is described for providing a variety of different emulsifiers or aqueous dispersant
Head tank is for storing raw material to be emulsified, and the liquid feed device is connected with liquid feeding pipeline, and the head tank is connected with raw material pipeline,
The raw material pipeline and the liquid feeding pipeline are connect with the input terminal of the emulsification, dispersal device；The emulsification, dispersal device
Output end connect with the import of the intermediate buffer tank by connecting line, the outlet of the intermediate buffer tank connects described defeated
Pipeline out.
2. the device of continuous production emulsion according to claim 1, it is characterised in that: the liquid feed device includes dispersion
Tank and multiple original fluid containers are respectively provided with different types of emulsifier or dispersing agent in each original fluid container；The original fluid container is logical
It crosses control valve, flowmeter and metering pump to connect with the import of the dispersion tank, the outlet of the dispersion tank connects the feed flow
Pipeline；The top of the dispersion tank is additionally provided with hot water inlet connection hot-water cylinder, for providing hot water.
3. the device of continuous production emulsion according to claim 2, it is characterised in that: successively set on the raw material pipeline
It is equipped with control valve, flowmeter, filter and metering pump；Control valve, flowmeter, filter are disposed on the liquid feeding pipeline
And metering pump.
4. the device of continuous production emulsion according to claim 1, it is characterised in that: the head tank, dispersion tank and
The outlet of intermediate buffer tank is also respectively connected with blow-off valve, and the raw material pipeline and the liquid feeding pipeline are close to the emulsification, dispersion
The side of device is again provided with blow-off valve.
5. the device of continuous production emulsion according to claim 3, it is characterised in that: the hot-water cylinder is connected with hot water
Supervisor, the hot water main pipe are equipped with control valve, flowmeter and metering pump；The hot water main pipe is also connected with two-way hot water branch
Pipe, connect with the hot water inlet of the dispersion tank, the control valve being arranged in another way and the raw material pipeline is connect all the way；It is described
Connecting line is connected with two-way by control valve and connects branch, and the import of the connection branch and the intermediate buffer tank connects all the way
It connects, another way is connect with the output pipe close to one end of the intermediate buffer tank；The output pipe be provided with control valve,
Flowmeter and metering pump, the output pipe are additionally provided with circuit and connect with the intermediate buffer tank, hot-water cylinder.
6. the device of continuous production emulsion according to claim 5, it is characterised in that: the emulsification, dispersal device are set
It is equipped with multiple；The emulsification, dispersal device use mulser, homogenizer or Homogenizing pump；It is described emulsification, dispersal device output end
Glass peephole is provided on the connecting line of connection.
7. the device of continuous production emulsion according to claim 1 or 6, it is characterised in that: the raw material packet to be emulsified
Including paraffin, the emulsifier or dispersing agent of the emulsifier or aqueous dispersant include lignosulfonates and/or polyvinyl alcohol,
By weight, 40~60 parts of paraffin, emulsifier or 1~5 part of dispersing agent, 40~60 parts of water.
8. the device of continuous production emulsion according to claim 1, it is characterised in that: the continuous production emulsion
Device is set in a set casing body.
9. a kind of method of continuous production emulsion, it is characterised in that: the following steps are included:
1) by raw material heating and melting to be emulsified at liquid, and raw material liq to be emulsified is pumped into head tank by feeding pump；
2) water in hot-water cylinder is heated to 80-90 DEG C, and be added in dispersion tank；
3) as needed, select emulsifier or dispersing agent, and by specified original fluid container emulsifier or dispersing agent added according to ratio
Enter into dispersion tank, and be dissolved into hot water, forms emulsifier or aqueous dispersant；
4) according to the partial size of emulsion finished product and cut mode selection emulsification, dispersal device, and by raw material pipeline and feed flow
The emulsification of pipeline and selection, dispersal device connection；
5) liquid raw material to be emulsified and emulsifier or aqueous dispersant are extracted by predetermined ratio, and passes through emulsification, dispersal device
Carrying out physical mixed dispersion becomes emulsion；
6) emulsion processed is pumped into intermediate buffer tank；
7) emulsion in intermediate buffer tank is delivered to by subsequent production line by output pipe.
10. the method for continuous production emulsion according to claim 9, it is characterised in that: to be emulsified in the step 1)
Raw material is paraffin, and heating temperature is 80-90 DEG C；Emulsifier or dispersing agent are lignosulfonates and/or gather in the step 3)
Vinyl alcohol.
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| CN201910201571.4A CN109908778A (en) | 2019-03-18 | 2019-03-18 | A kind of device and method of continuous production emulsion |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110449051A (en) * | 2019-07-03 | 2019-11-15 | 全球能源互联网欧洲研究院 | A kind of continuous production system and method for phase transformation lotion |
Citations (11)
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| CN110449051B (en) * | 2019-07-03 | 2022-08-23 | 全球能源互联网欧洲研究院 | Continuous production system and method of phase-change emulsion |
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