CN207307678U - A kind of nucleator mixing system device - Google Patents
A kind of nucleator mixing system device Download PDFInfo
- Publication number
- CN207307678U CN207307678U CN201721109198.2U CN201721109198U CN207307678U CN 207307678 U CN207307678 U CN 207307678U CN 201721109198 U CN201721109198 U CN 201721109198U CN 207307678 U CN207307678 U CN 207307678U
- Authority
- CN
- China
- Prior art keywords
- pipe
- autoclave body
- water
- emulsification
- heat exchange
- 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
- 238000002156 mixing Methods 0.000 title claims abstract description 20
- 238000004945 emulsification Methods 0.000 claims abstract description 41
- 239000000463 material Substances 0.000 claims abstract description 33
- 230000001804 emulsifying effect Effects 0.000 claims abstract description 27
- 238000003756 stirring Methods 0.000 claims abstract description 12
- 238000003466 welding Methods 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 117
- 239000002918 waste heat Substances 0.000 claims description 31
- 238000011084 recovery Methods 0.000 claims description 30
- 239000007788 liquid Substances 0.000 claims description 20
- 238000000926 separation method Methods 0.000 claims description 19
- 238000005192 partition Methods 0.000 claims description 15
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 6
- 230000000740 bleeding effect Effects 0.000 claims description 6
- 229910052802 copper Inorganic materials 0.000 claims description 6
- 239000010949 copper Substances 0.000 claims description 6
- 230000008878 coupling Effects 0.000 claims description 4
- 238000010168 coupling process Methods 0.000 claims description 4
- 238000005859 coupling reaction Methods 0.000 claims description 4
- 238000005086 pumping Methods 0.000 claims description 4
- 238000007789 sealing Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims 1
- 230000005611 electricity Effects 0.000 claims 1
- 230000000694 effects Effects 0.000 description 5
- 239000013078 crystal Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 239000011344 liquid material Substances 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Abstract
The utility model discloses a kind of nucleator mixing system device, including emulsifying autoclave body, charge pipe is installed at the top of the emulsification autoclave body, the outer tip position of emulsification autoclave body is installed with horizontally disposed installing plate by the form of welding, stirring motor is wherein provided with by screw on installing plate, it is shorter that the utility model preheats the required time, so as to more energy saving, so batch mixing can be quickly carried out again after emulsifying kettle body materials inside clean-drain, rerolling required preheating time is so greatly reduced, it is overall comparatively more efficient.
Description
Technical field
Field of chemical equipment is the utility model is related to, more particularly, to a kind of nucleator mixing system device.
Background technology
Nucleator applies to the imperfect crystal plastics such as polyethylene, polypropylene, by varying the crystallization behavior of resin, adds
Fast crystalline rate, increase crystal density and promote fine grain size, reach shorten molding cycle, improve the product transparency,
The new function of the physical mechanical properties such as lustrous surface, tensile strength, rigidity, heat distortion temperature, impact resistance, creep resistance helps
Agent.
Existing nucleator mixing device needs certain preheating time in rerolling, not only needs certain consumption at this time
Can, and batch mixing is discontinuous, so that efficiency is very low.
Utility model content
The utility model is to overcome the above situation insufficient, it is desirable to provide a kind of technical solution that can be solved the above problems.
A kind of nucleator mixing system device, including emulsification autoclave body, described emulsify are provided with charge pipe at the top of autoclave body, breast
The outer tip position for changing autoclave body is installed with horizontally disposed installing plate by the form of welding, wherein passes through spiral shell on installing plate
Silk is provided with stirring motor, and the motor shaft of stirring motor through the through hole at the top of installing plate and emulsification autoclave body and extends to emulsification
On the inside of autoclave body, and the bottom position of motor shaft is connected with by shaft coupling and is vertically arranged agitating shaft, and agitating shaft is arranged on emulsification autoclave body
Inner side, and the bottom of agitating shaft is welded with turbo blade, drives agitating shaft to rotate by stirring motor, so as to fulfill turbine leaf
Stirring of the piece to material；Emulsifying machine head is cased with the outside of the turbo blade, and emulsifying machine head is connected by vertical emulsifying machine head
Bar is welded to connect installing plate, emulsifies and is provided with electrothermal tube by screw on the inner wall of autoclave body, and the power cord of electrothermal tube is from emulsification
String holes on autoclave body outer wall is pierced by, and sealing is injected with string holes；Waste heat recovery water is enclosed with the outer wall of the emulsification autoclave body
Set, wherein the top of waste heat recovery water jacket and bottom are connected to water inlet pipe and return pipe, by waste heat recovery water
Water filling in set, the heat that the water absorption external wall of emulsifying kettle in waste heat recovery water jacket is come out at this time；The emulsification autoclave body
Bottom discharge mouth be welded with discharge nozzle, and outlet valve is installed on discharge nozzle；The end of discharge nozzle, which is also accessed, is provided with auger
Conveyer；Bleeding point is offered at the top of the emulsification autoclave body, and bleeding point connects the pumping end of aspiration pump by exhaust tube, leads to
The effect using aspiration pump is crossed, the gas produced inside emulsifying kettle body can quickly be taken away, avoids occurring inside emulsifying kettle body
The situation of high pressure；The another of the water inlet pipe is terminated on the water inlet of liquid separation disk, and the liquid separation disk, which is bolted to, to be changed
In hot tank, liquid separation disk is in hollow structure, and the lower surface of liquid separation disk offers multiple water outlets, and wherein water outlet docks respectively
There are the heat exchanging water pipe being vertically arranged, heat exchanging water pipe's bottom opening, and be arranged at intervals between heat exchanging water pipe, welding in the heat exchange box
Horizontally disposed partition plate is fixed with, the bottom of heat exchanging water pipe is worn to the lower position of partition plate, and is adopted between heat exchanging water pipe and partition plate
Fixed and sealed with the form of welding；The left side wall gating location of the heat exchange box is connected to feed pipe, the right side of the heat exchange box
Side wall discharge port connects charge pipe, and metering pump is provided with charge pipe, wherein the feed inlet of heat exchange box and discharge port be respectively positioned on every
The top position of plate, and feed inlet is located at the top position of discharge port, the left side wall water return outlet of heat exchange box takes back water pipe, and exchanges heat
The lower position of the water return outlet partition plate of case, is provided with suction pump on return pipe, and in actual use, emulsification autoclave body gives out
The preheating come is progressively absorbed by the water in waste heat recovery water jacket, is at this time pumped heat exchange box to waste heat recovery water using suction pump
In set, realize exchange heat between the water in waste heat recovery water jacket and the outer wall for emulsifying autoclave body at this time, at the same it is remaining under the action of hydraulic pressure
Hot water is transported to liquid separation disk at water inlet pipe in recuperation of heat water jacket, and then hot water is dispersed into heat exchanging water pipe through liquid separation disk,
Heat exchanging water pipe can be heated by hot water at this time, while heat exchanging water pipe is emitted into heat exchange box from bottom end outlet, so can be real
Existing cycle heat exchange between waste heat recovery water jacket and heat exchange box, is delivered to heat exchanging water pipe's at feed pipe by liquid material at this time
Top position, and material is contacted and exchanged heat with heat exchanging water pipe, effect of the heated material through charge pipe and metering pump is sent
Enter and be mixed in emulsifying kettle body, metering pump realizes quantitative taking at this time, and material can be very good to keep away by preliminary preheating
Exempt from material and excessively sticky situation occur, such material can be presented certain temperature before emulsification autoclave body is sent into, at this time will
The material feeding emulsification autoclave body preheating required time is shorter, thus it is more energy saving, so cleaned in emulsifying kettle body materials inside
Batch mixing can be quickly carried out after emptying again, so greatly reduces rerolling required preheating time, it is overall to come relatively
Say more efficient.
As further program of the utility model：Water valve is mounted on the water inlet pipe and return pipe.
As further program of the utility model：The waste heat recovery water jacket is made of copper material, and waste heat recovery water
The edge placement of set is connected and sealed with the outer wall of emulsification autoclave body using the form of welding.
As further program of the utility model：The heat exchanging water pipe is used and is made of copper material.
As further program of the utility model：The bottom of the emulsification autoclave body is welded with column.
As further program of the utility model：Inlet valve is installed on the charge pipe.
The beneficial effects of the utility model：The utility model preheating required time is shorter, thus it is more energy saving, so
Batch mixing can be quickly carried out again after emulsifying kettle body materials inside clean-drain, required for so greatly reducing rerolling
Preheating time, it is overall comparatively more efficient.
The additional aspect and advantage of the utility model will be set forth in part in the description, partly by from following description
In become obvious, or recognized by the practice of the utility model.
Brief description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property
Put, other attached drawings can also be obtained according to these attached drawings.
Fig. 1 is the utility model structure diagram；
Fig. 2 is the partial structural diagram of the utility model.
In figure：1- emulsification autoclave body, 2- columns, 3- charge pipes, 4- discharge nozzles, 5- outlet valves, 6- inlet valves, 7- installing plates,
8- stirring motors, 9- shaft couplings, 10- agitating shafts, 11- emulsifying machine heads, 12- waste heat recoveries water jacket, 13- return pipes, 14- water inlets
Pipe, 15- water valves, 16- electrothermal tubes, 17- emulsifying machine heads connecting rod, 18- aspiration pumps, 19- screw conveyors, 20- suction pumps, 21- are changed
Hot tank, 22- partition plates, 23- heat exchanging water pipes, 24- exhaust tubes, 25- liquid separations disk, 26- feed pipes, 27- metering pumps, 28- water outlets.
Embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained, shall fall within the protection scope of the present invention.
Please refer to Fig.1~2, in the utility model embodiment, a kind of nucleator mixing system device, including emulsification autoclave body 1,
The top of the emulsification autoclave body 1 is provided with charge pipe 3, and the outer tip position for emulsifying autoclave body 1 is fixedly mounted by the form of welding
There is horizontally disposed installing plate 7, stirring motor 8 is provided with by screw wherein on installing plate 7, the motor shaft of stirring motor 8 is worn
Cross installing plate 7 and emulsify the through hole at the top of autoclave body 1 and extend to 1 inner side of emulsification autoclave body, and the bottom position of motor shaft passes through
Shaft coupling 9, which is connected with, is vertically arranged agitating shaft 10, and agitating shaft 10 is arranged on the inner side of emulsification autoclave body 1, and the bottom weldering of agitating shaft 10
Turbo blade is connected to, drives agitating shaft 10 to rotate by stirring motor 8, so as to fulfill stirring of the turbo blade to material；It is described
Emulsifying machine head 11 is cased with the outside of turbo blade, and emulsifying machine head 11 is welded to connect installation by vertical emulsifying machine head connecting rod 17
Plate 7, emulsifies and is provided with electrothermal tube 16 by screw on the inner wall of autoclave body 1, and the power cord of electrothermal tube 16 is from emulsification 1 outer wall of autoclave body
On string holes be pierced by, and sealing is injected with string holes；Waste heat recovery water jacket 12 is enclosed with the outer wall of the emulsification autoclave body 1, its
The top and bottom of middle waste heat recovery water jacket 12 are connected to water inlet pipe 14 and return pipe 13, by waste heat recovery water
Water filling in set 12, the water in waste heat recovery water jacket 12, which absorbs, at this time emulsifies the heat that 1 outer wall of autoclave body is come out；The emulsification
The bottom discharge mouth of autoclave body 1 is welded with discharge nozzle 4, and outlet valve 5 is provided with discharge nozzle 4；Peace is also accessed in the end of discharge nozzle 4
Equipped with screw conveyor 19；The top of the emulsification autoclave body 1 offers bleeding point, and bleeding point is connected by exhaust tube 24 and is evacuated
The pumping end of pump 18, the gas for emulsifying the generation of the inside of autoclave body 1 by using the effect of aspiration pump 18, can quickly be taken away, kept away
Exempt to emulsify inside autoclave body 1 and the situation of high pressure occur；The another of the water inlet pipe 14 is terminated on the water inlet of liquid separation disk 25, described
Liquid separation disk 25 is bolted in heat exchange box 21, and liquid separation disk 25 is in hollow structure, and the lower surface of liquid separation disk 25 opens up
There are multiple water outlets 28, wherein water outlet 28 is respectively to being connected to the heat exchanging water pipe 23 being vertically arranged, 23 bottom opening of heat exchanging water pipe,
And be arranged at intervals between heat exchanging water pipe 23, horizontally disposed partition plate 22 is welded with the heat exchange box 21, heat exchanging water pipe 23
Bottom wear to the lower position of partition plate 22, and fix and seal in the form of welding between heat exchanging water pipe 23 and partition plate 22；
The left side wall gating location of the heat exchange box 21 is connected to feed pipe 26, and the right side wall discharge port of the heat exchange box 21 connects charge pipe
3, and metering pump 27 is installed on charge pipe 3, wherein the feed inlet of heat exchange box 21 is respectively positioned on the upper position of partition plate 22 with discharge port
To put, and feed inlet is located at the top position of discharge port, the left side wall water return outlet of heat exchange box 21 takes back water pipe 13, and heat exchange box 21
The lower position of water return outlet partition plate 22, is provided with suction pump 20 on return pipe 13, and in actual use, emulsification autoclave body 1 dissipates
The preheating issued is progressively absorbed by the water in waste heat recovery water jacket 12, at this time using suction pump 20 by heat exchange box 21 pump to
In waste heat recovery water jacket 12, realize exchange heat between the water in waste heat recovery water jacket 12 and the outer wall for emulsifying autoclave body 1 at this time, while
Hot water is transported to liquid separation disk 25 at water inlet pipe 14 in waste heat recovery water jacket 12 under the action of hydraulic pressure, and then hot water is through liquid separation disk
25 are dispersed into heat exchanging water pipe 23, and heat exchanging water pipe 23 can be heated by hot water at this time, while heat exchanging water pipe 23 goes out from bottom
Mouthful be emitted into heat exchange box 21, can so realize the cycle heat exchange between waste heat recovery water jacket 12 and heat exchange box 21, at this time from
Liquid material is delivered to the top position of heat exchanging water pipe 23 at feed pipe 26, and material is contacted and exchanged heat with heat exchanging water pipe 23,
Effect of the heated material through charge pipe 3 and metering pump 27 is admitted in emulsification autoclave body 1 and is mixed, and measures at this time
Pump 27 realizes quantitative taking, and material can be very good to avoid material from excessively sticky situation, such thing occur by preliminary preheating
Certain temperature can be presented before emulsification autoclave body 1 is sent into material, when material feeding emulsification autoclave body 1 being preheated required at this time
Between it is shorter so that more energy saving, so can quickly carry out batch mixing again after 1 materials inside clean-drain of autoclave body is emulsified, this
Sample greatly reduces rerolling required preheating time, overall comparatively more efficient.
Water valve 15 is mounted on the water inlet pipe 14 and return pipe 13.
The waste heat recovery water jacket 12 is made of copper material, and the edge placement of waste heat recovery water jacket 12 is using the shape of welding
Formula is connected and seals with the outer wall of emulsification autoclave body 1.
The heat exchanging water pipe 23 is used and is made of copper material.
The bottom of the emulsification autoclave body 1 is welded with column 2.
Inlet valve 6 is installed on the charge pipe 3.
The operation principle of the utility model is：In actual use, the preheating that comes out of emulsification autoclave body 1 progressively by
Water in waste heat recovery water jacket 12 is absorbed, and is at this time pumped heat exchange box 21 to waste heat recovery water jacket 12 using suction pump 20,
Realize and exchange heat between the water in waste heat recovery water jacket 12 and the outer wall for emulsifying autoclave body 1 at this time, while the waste heat under the action of hydraulic pressure
Hot water is transported to liquid separation disk 25 at water inlet pipe 14 in recycling water jacket 12, and then hot water is dispersed into heat-exchanging water through liquid separation disk 25
In pipe 23, heat exchanging water pipe 23 can be heated by hot water at this time, while heat exchanging water pipe 23 is emitted into heat exchange box 21 from bottom end outlet
It is interior, the cycle heat exchange between waste heat recovery water jacket 12 and heat exchange box 21 can be so realized, at this time by liquid at feed pipe 26
Material is delivered to the top position of heat exchanging water pipe 23, and material is contacted and exchanged heat with heat exchanging water pipe 23, and heated material is through adding
The effect of expects pipe 3 and metering pump 27 is admitted in emulsification autoclave body 1 and is mixed, and metering pump 27 realizes quantitative at this time
Material, and material can be very good to avoid material from excessively sticky situation occur by preliminary preheating, such material is being sent into emulsifying kettle
Certain temperature can be presented before body 1, material is sent into emulsification autoclave body 1 at this time, and to preheat the required time shorter, so that more
Supernumerary segment energy, so can quickly carry out batch mixing again after 1 materials inside clean-drain of autoclave body is emulsified, so greatly reduce two
It is secondary batch mixing required preheating time, overall comparatively more efficient.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and
And in the case of the spirit or essential attributes without departing substantially from the utility model, it can realize that this practicality is new in other specific forms
Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this practicality is new
The scope of type is indicated by the appended claims rather than the foregoing description, it is intended that the equivalency fallen in claim is contained
All changes in justice and scope are embraced therein.Any reference numeral in claim should not be considered as limitation
Involved claim.
Claims (6)
1. a kind of nucleator mixing system device, including emulsification autoclave body, described emulsify is provided with charge pipe at the top of autoclave body, emulsifies
The outer tip position of autoclave body is installed with horizontally disposed installing plate by the form of welding, wherein passes through screw on installing plate
Stirring motor is installed, the motor shaft of stirring motor through the through hole at the top of installing plate and emulsification autoclave body and extends to emulsifying kettle
Internal side, and the bottom position of motor shaft is connected with by shaft coupling and is vertically arranged agitating shaft, agitating shaft is arranged on emulsification autoclave body
Inner side, and the bottom of agitating shaft is welded with turbo blade；Emulsifying machine head is cased with the outside of the turbo blade, and emulsifying machine head leads to
Cross vertical emulsifying machine head connecting rod and be welded to connect installing plate, emulsify and electrothermal tube, and electricity are provided with by screw on the inner wall of autoclave body
The power cord of heat pipe is pierced by from the string holes on the external wall of emulsifying kettle, and sealing is injected with string holes；It is characterized in that, the emulsification
Waste heat recovery water jacket is enclosed with the outer wall of autoclave body, the wherein top of waste heat recovery water jacket and bottom is connected to water inlet pipe
And return pipe；The bottom discharge mouth of the emulsification autoclave body is welded with discharge nozzle, and outlet valve is provided with discharge nozzle；Discharge nozzle
End also access screw conveyor be installed；Bleeding point is offered at the top of the emulsification autoclave body, and bleeding point passes through pumping
Pipe connects the pumping end of aspiration pump；The another of the water inlet pipe is terminated on the water inlet of liquid separation disk, and the liquid separation disk uses spiral shell
Bolt is fixed in heat exchange box, and liquid separation disk is in hollow structure, and the lower surface of liquid separation disk offers multiple water outlets, wherein water outlet
Mouth is described to change respectively to being connected to the heat exchanging water pipe being vertically arranged, heat exchanging water pipe's bottom opening, and be arranged at intervals between heat exchanging water pipe
Be welded with horizontally disposed partition plate in hot tank, the bottom of heat exchanging water pipe is worn to the lower position of partition plate, and heat exchanging water pipe with
Fix and seal in the form of welding between partition plate；The left side wall gating location of the heat exchange box is connected to feed pipe, described
The right side wall discharge port of heat exchange box connects charge pipe, and metering pump is provided with charge pipe, wherein the feed inlet of heat exchange box and discharging
Mouth is respectively positioned on the top position of partition plate, and feed inlet is located at the top position of discharge port, and the left side wall water return outlet of heat exchange box takes back
Water pipe, and the lower position of the water return outlet partition plate of heat exchange box, are provided with suction pump on return pipe.
2. nucleator mixing system device according to claim 1, it is characterised in that on the water inlet pipe and return pipe
It is mounted on water valve.
3. nucleator mixing system device according to claim 1, it is characterised in that the waste heat recovery water jacket uses copper
Material is made, and the edge placement of waste heat recovery water jacket is connected and sealed with the outer wall of emulsification autoclave body using the form of welding.
4. nucleator mixing system device according to claim 1, it is characterised in that the heat exchanging water pipe uses copper
Material is made.
5. nucleator mixing system device according to claim 1, it is characterised in that the bottom welding of the emulsification autoclave body
There is column.
6. nucleator mixing system device according to claim 1, it is characterised in that charging is provided with the charge pipe
Valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721109198.2U CN207307678U (en) | 2017-08-31 | 2017-08-31 | A kind of nucleator mixing system device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721109198.2U CN207307678U (en) | 2017-08-31 | 2017-08-31 | A kind of nucleator mixing system device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207307678U true CN207307678U (en) | 2018-05-04 |
Family
ID=62384984
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721109198.2U Expired - Fee Related CN207307678U (en) | 2017-08-31 | 2017-08-31 | A kind of nucleator mixing system device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207307678U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111111502A (en) * | 2019-12-31 | 2020-05-08 | 无锡安鑫卓越智能科技有限公司 | Novel double-shaft heating and solidifying liquid type stirring machine |
-
2017
- 2017-08-31 CN CN201721109198.2U patent/CN207307678U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111111502A (en) * | 2019-12-31 | 2020-05-08 | 无锡安鑫卓越智能科技有限公司 | Novel double-shaft heating and solidifying liquid type stirring machine |
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|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180504 Termination date: 20200831 |
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| CF01 | Termination of patent right due to non-payment of annual fee |