CN108162234A - The method for solving the fervent high-viscosity material particle agglomeration phenomenon of die face - Google Patents
The method for solving the fervent high-viscosity material particle agglomeration phenomenon of die face Download PDFInfo
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- CN108162234A CN108162234A CN201711426413.6A CN201711426413A CN108162234A CN 108162234 A CN108162234 A CN 108162234A CN 201711426413 A CN201711426413 A CN 201711426413A CN 108162234 A CN108162234 A CN 108162234A
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- 239000002245 particle Substances 0.000 title claims abstract description 86
- 239000000463 material Substances 0.000 title claims abstract description 56
- 238000000034 method Methods 0.000 title claims abstract description 21
- 238000005054 agglomeration Methods 0.000 title claims abstract description 18
- 230000002776 aggregation Effects 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 81
- 238000005461 lubrication Methods 0.000 claims abstract description 27
- 238000001816 cooling Methods 0.000 claims description 21
- 238000004062 sedimentation Methods 0.000 claims description 17
- 238000012216 screening Methods 0.000 claims description 6
- 239000004698 Polyethylene Substances 0.000 abstract description 6
- 239000011248 coating agent Substances 0.000 abstract description 6
- 238000000576 coating method Methods 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- -1 polyethylene Polymers 0.000 abstract description 6
- 229920000573 polyethylene Polymers 0.000 abstract description 6
- 238000005453 pelletization Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 230000033001 locomotion Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 206010057071 Rectal tenesmus Diseases 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000036760 body temperature Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000002262 irrigation Effects 0.000 description 1
- 238000003973 irrigation Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 208000012271 tenesmus Diseases 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
- B29B9/065—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion under-water, e.g. underwater pelletizers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/04—Conditioning or physical treatment of the material to be shaped by cooling
- B29B13/045—Conditioning or physical treatment of the material to be shaped by cooling of powders or pellets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/06—Conditioning or physical treatment of the material to be shaped by drying
- B29B13/065—Conditioning or physical treatment of the material to be shaped by drying of powder or pellets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/10—Conditioning or physical treatment of the material to be shaped by grinding, e.g. by triturating; by sieving; by filtering
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/16—Auxiliary treatment of granules
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The present invention relates to prilling technical fields, the method for especially solving the fervent high-viscosity material particle agglomeration phenomenon of die face, this method is to provide an air-cooled environment for breaing up particle based on water lubrication, the high-viscosity material particle that die face earnestly obtains is allowed to enter the environment, the particle come out by the environment is the stable state being separated from each other, finally using water ring section is removed, the smooth material particles in surface are obtained;The air-cooled environment for breaing up particle based on water lubrication is built by the cone cylinder of a vertical setting, cone cylinder epimere is equipped with side feed opening and connects air-cooled feeding passage, water inlet pipe is introduced at the top of cone cylinder, cone cylinder bottom is equipped with cone mouth connection primary vibration sieve, and primary vibration sieve realizes that material particles are separated from water.The high-viscosity material particle that the present invention allows die face earnestly to obtain is separated from each other, and finally using water ring section is removed, obtains the smooth material particles in surface, solves and die face fervent particle agglomeration phenomenon is caused due to polyethylene coating materials viscosity is big, improve production efficiency.
Description
Technical field
The present invention relates to the technical fields of the fervent high-viscosity material particle of prilling technical field, especially die face.
Background technology
Being granulated industry has a kind of granulation mode to claim mould face air cooling pelletizing, and this technology is mainly for hygroscopic or be not easy
Dehydration and drying and moisture easily cause product quality dysgenic material to be granulated.But in enterprise production process
A large amount of polyethylene coating materials of generation be granulated again and are recycled, and are exactly viscosity due to being granulated the characteristics of protruding with polyethylene coating materials
Greatly, pelletizing is carried out to polyethylene coating materials using the fervent technology of die face, often will appear particle agglomeration during die face is earnestly covered, it is defeated
Particle line clogging phenomenon is sent, the fervent pelletizing speed of die face can only be reduced because die face earnestly generates particle agglomeration phenomenon by alleviating
Degree, therefore production efficiency is low.
Invention content
The purpose of the present invention is to provide the methods for solving the fervent high-viscosity material particle agglomeration phenomenon of die face, promote production
Efficiency, suitable for carrying out pelletizing production to polyethylene coating materials.
In order to achieve the above objectives, the present invention adopts the following technical scheme that:
The method for solving the fervent high-viscosity material particle agglomeration phenomenon of die face, this method are to provide one based on the air-cooled of water lubrication
The environment of particle is broken up, the high-viscosity material particle that die face earnestly obtains is allowed to enter the environment, the particle come out by the environment
For the stable state being separated from each other, finally using water ring section is removed, the smooth material particles in surface are obtained.
Said program is further:The particle itself come out by the air-cooled environment for breaing up particle based on water lubrication
Temperature is controlled at 30 ~ 40 DEG C.
Said program is further:The air-cooled environment for breaing up particle based on water lubrication is an enclosed environment, and logical
The air-cooled feeding passage connection fervent station of die face of closing is crossed, air-cooled feeding passage provides whirlwind by wind turbine.
Said program is further:The air-cooled environment for breaing up particle based on water lubrication is by the cone of a vertical setting
Cylinder is built, and cone cylinder epimere is equipped with side feed opening and connects air-cooled feeding passage, and water inlet pipe, the water outlet of water inlet pipe are introduced at the top of cone cylinder
End is less than side feed opening;Cone cylinder bottom is equipped with cone mouth connection primary vibration sieve, and primary vibration sieve realizes material particles and moisture
From.
Said program is further:The primary vibration sieve is equipped with three layer screen and is layered, and upper two layers are particle screening layer,
Bottom is lubrication moisture screen layers;The lubrication moisture screen layers connect circulating cooling system, which supplies water to water inlet pipe;
The upper two layers particle screening layer drops into material particles vibrating screen in conveying charging basket, and water ring is removed using based on air-cooled
Section processing.
Said program is further:The fervent station of die face is equipped with earnestly cover, and the tangential direction for earnestly covering bottom is equipped with
The air inlet and air outlet of one word connection, air inlet connect wind turbine by ripple ajutage, and wind turbine is with adjusting air-supply rotation
The centrifugal fan of lid, the air outlet of wind turbine are higher than the 160 ~ 200mm of air inlet earnestly covered, and the air outlet earnestly covered is then
Connect air-cooled feeding passage.
Said program is further:The circulating cooling system includes the first sedimentation basin, the second sedimentation basin, cooling column, storage
Pond;First sedimentation basin receives the water of lubrication moisture screen layers outflow, the second sedimentation basin by pipeline be connected to the first sedimentation basin and
Between cooling column, the water after cooling column cooling treatment is stored in cistern, and cistern connects water inlet pipe, water inlet pipe by water pump
It is equipped with control water valve.
Said program is further:The fervent station of die face is equipped with the anti-blade on knife rest, knife rest connection heat
Cut the output shaft of motor.
Air-cooled the present invention is based on water lubrication breaks up particle, and the high-viscosity material particle that die face earnestly obtains is allowed mutually to divide
From finally using water ring section is removed, the smooth material particles in acquisition surface solve and cause mould due to polyethylene coating materials viscosity is big
The fervent particle agglomeration phenomenon in face improves production efficiency.And also comply with and hygroscopic modified material is granulated, turn off for water system
System can switch granulation mode at any time, and multipurpose can be promoted the use of, and have certain economy and practicability.
Description of the drawings:
Process flow chart of the attached drawing 1 for the present invention;
The one apparatus embodiments structure diagram that attached drawing 2 is used for the present invention;
Attached drawing 3 is Fig. 2 embodiment construction profiles;
Attached drawing 4 is Fig. 2 embodiment overlooking structure figures;
Attached drawing 5 is Fig. 2 embodiment part-structure exploded views.
Specific embodiment:
Below with reference to design of the attached drawing to the present invention, the technique effect that concrete structure generates is described further, with abundant
Ground understands the purpose of invention, feature and effect.
As shown in fig.1, for present invention process flow chart, a kind of related solution fervent high-viscosity material of die face of the present invention
The method of grain agglomeration, this method are to provide an air-cooled environment for breaing up particle based on water lubrication, die face are allowed earnestly to obtain
High-viscosity material particle enter the environment, the particle come out by the environment is the stable state that is separated from each other, finally using
Water ring section is removed, obtains the smooth material particles in surface.Raw material are conveyed after mixing by elevator, by double-cone feeding and with
Modified material is with rotating speed feeding, and then progress die face is fervent, and the high-viscosity material particle that die face earnestly obtains enters to be moistened based on water
The sliding air-cooled environment for breaing up particle, under the action of whirlwind, particle turn and under water lubrication realize break up, detach, in this way,
The particle come out by the environment is the stable state being separated from each other, it is preferable that passes through the air-cooled ring for breaing up particle based on water lubrication
Border come out particle own temperature control at 30 ~ 40 DEG C, surface moisture is evaporated by material particles own temperature, then using
Air-cooled and vibrating screen grades water ring section, realizes the essentially dry no moisture of material particles, and particle surface is smooth;Finally carrying out
The operations such as packaging and storage.
Refering to shown in Fig. 2 ~ 5, in the present embodiment, the air-cooled environment for breaing up particle based on water lubrication is a closed-loop
Border, and the fervent station of die face is connected by the air-cooled feeding passage 3 of closing, air-cooled feeding passage provides whirlwind by wind turbine 2.It is described
The air-cooled environment for breaing up particle based on water lubrication is built by the cone cylinder 1 of a vertical setting, and 1 epimere of cone cylinder is equipped with side-fed
The 11 air-cooled feeding passages 3 of connection of mouth, 1 top of cone cylinder introduce water inlet pipe 4, and the water outlet of water inlet pipe 4 is less than side feed opening 11;Cone
11 bottoms of cylinder are equipped with cone mouth connection primary vibration sieve 5, and 5 realization material particles of primary vibration sieve are separated from water.In the present embodiment, institute
It states primary vibration sieve 5 and is equipped with three layer screen layering, upper two layers are particle screening layer 51,52, and bottom is lubrication moisture screen layers 53;
The lubrication moisture screen layers 53 connect circulating cooling system 6, which supplies water to water inlet pipe 4.The upper two layers
Grain screening layered 51,52 rotates transmission and drops into material particles vibrating screen in conveying charging basket 54 successively, and conveying charging basket 54 exports
Material particles go water ring section to handle using based on air-cooled, reach particle surface lubricous dry, without being separately dried.
Shown in Fig. 2 ~ 5, in the present embodiment, the fervent station of die face is equipped with earnestly cover 7, earnestly covers the tangent line side of 7 bottoms
To the air inlet 71 and air outlet 72 connected equipped with a word, air inlet 71 connects wind turbine 2 by ripple ajutage 73, and wind turbine 2 is
With the centrifugal fan for adjusting air-supply swivelling cover 21, the air outlet of wind turbine 2 is higher than the 160 ~ 200mm of air inlet earnestly covered,
An angle is tilted naturally after air-supply corrugated flexible hose connection in this way, to sending lower whirlwind in fervent cover.The outlet air earnestly covered
Mouth 72 then connects air-cooled feeding passage 3, and there is the negative direction welding up and down of 45o elbows at air-cooled 3 both ends of feeding passage, and satisfaction makes particle defeated
Distance is short when sending, while realizes that material particles climbs from lower to upper in air-cooled feeding passage 3 and move and from the side of cone cylinder epimere
Face feed inlet 11 enters in cone cylinder 1, forms eddying motion.
Shown in Fig. 2 ~ 5, in the present embodiment, the circulating cooling system 6 include the first sedimentation basin 61, the second sedimentation basin 62,
Cooling column 63, cistern 64;First sedimentation basin 61 receives the water of 53 outflow of lubrication moisture screen layers, and the second sedimentation basin 62 passes through pipeline
It is connected between the first sedimentation basin 62 and cooling column 63, the water after 63 cooling treatment of cooling column is stored in cistern 64, water storage
Pond 64 connects water inlet pipe 4 by water pump, and water inlet pipe 4 is equipped with control water valve 41, thus controls water or closes water inlet etc..It is described
The fervent station of die face is equipped with the anti-blade 81 on knife rest 8, and knife rest 8 connects the output shaft of fervent motor 9.
Shown in Fig. 2 ~ 5, in the present embodiment, wind turbine 2, ripple ajutage 73, earnestly cover 7, air-cooled feeding passage 3, in cone cylinder
The side feed opening 11 of section is connected on same center line, is locked with manual junction button, realizes accessible feeding.Material from
It is fervent by 81 die face of blade on the fervent station of die face after being squeezed out in foraminous die plate, it is possible to mould directly be carried out to fused materials
Face pelletizing simultaneously casts die face aside, passes through wind together with the lower whirlwind that wind turbine 2 is sent by centrifugal rotation, particle in fervent cover 11
Cold feeding passage 3, cone cylinder epimere side feed opening 11 be sent into cone cylinder 1 in.Material particles are with whirlwind from the side of cone cylinder epimere
Into in cone cylinder 1, the tenesmus movement that is vortexed is formed, at this moment, the control water valve 41 of water inlet pipe 4 is opened, inflow is controlled, by intaking
Pipe 4, which supplies water into cone cylinder 1, can play the role of to particle water lubrication.High-temperature material particle meets water and does lubricant, in wind turbine 2
Under the lower whirlwind effect being sent into, eddy flow is formd around 1 barrel of cone cylinder, is broken up high-temperature particle by cyclonic separation moment, quilt
The particle broken up and lubrication water together be slipped to primary vibration sieve 5 on.After 5 separation water of primary vibration sieve, material particles are certainly
There are about 30 DEG C -40 DEG C or so, then sieve drops into conveying charging basket 54 body temperature, evaporates surface moisture by own temperature, then
By water ring section being gone to handle based on air-cooled, the essentially dry no moisture of material particles, particle surface is smooth.Primary vibration sieve 5
The lubricating irrigation flow separated into the first sedimentation basin 61, be sent in cooling column 63 after water pipe flows into the second sedimentation basin 62 into
Row water cooling, cooling water are flowed back into cistern 64 and are continued cycling through.
In work, a small amount of vapor generated in cone cylinder 1 is connected to discharge outdoor on dust collecting duct by exhaust duct 12.Mould
Air output should not be too large during the fervent high-viscosity material in face, and the unlatching for swivelling cover 21 of being blown by adjusting controls air quantity, meets mould
The high-viscosity material particle that face earnestly obtains is sent into cone cylinder 1.In the present embodiment, the water outlet of water inlet pipe 4 is down to cone cylinder
At the 150mm of 11 lower section of side feed opening.
The present invention is elaborated above in association with embodiment, only technical concepts and features to illustrate the invention,
Its object is to which person skilled in the art is allowed to understand present disclosure and is implemented, it can not limit the present invention's with this
Protection domain, therefore all equivalent change or modifications done according to spirit of the invention should all cover the protection model in the present invention
In enclosing.
Claims (8)
1. solve the method for the fervent high-viscosity material particle agglomeration phenomenon of die face, it is characterised in that:This method is to provide a base
In the air-cooled environment for breaing up particle of water lubrication, the high-viscosity material particle that die face earnestly obtains is allowed to enter the environment, by this
The particle that environment comes out is the stable state being separated from each other, and finally using water ring section is removed, obtains the smooth material particles in surface.
2. the method according to claim 1 for solving the fervent high-viscosity material particle agglomeration phenomenon of die face, it is characterised in that:
The particle own temperature come out by the air-cooled environment for breaing up particle based on water lubrication is controlled at 30 ~ 40 DEG C.
3. the method according to claim 1 for solving the fervent high-viscosity material particle agglomeration phenomenon of die face, it is characterised in that:
The air-cooled environment for breaing up particle based on water lubrication is an enclosed environment, and connects mould by the air-cooled feeding passage of closing
The fervent station in face, air-cooled feeding passage provide whirlwind by wind turbine.
4. the method for the fervent high-viscosity material particle agglomeration phenomenon of solution die face according to claims 1 or 2 or 3, special
Sign is:The air-cooled environment for breaing up particle based on water lubrication is built by the cone cylinder of a vertical setting, and cone cylinder epimere is set
There is side feed opening to connect air-cooled feeding passage, water inlet pipe is introduced at the top of cone cylinder, the water outlet of water inlet pipe is less than side feed opening;
Cone cylinder bottom is equipped with cone mouth connection primary vibration sieve, and primary vibration sieve realizes that material particles are separated from water.
5. the method according to claim 4 for solving the fervent high-viscosity material particle agglomeration phenomenon of die face, it is characterised in that:
The primary vibration sieve is equipped with three layer screen and is layered, and upper two layers are particle screening layer, and bottom is lubrication moisture screen layers;The lubrication
Moisture screen layers connect circulating cooling system, which supplies water to water inlet pipe;The upper two layers particle screening layer will
Material particles vibrating screen is dropped into conveying charging basket, water ring section is gone to handle using based on air-cooled.
6. the method according to claim 3 for solving the fervent high-viscosity material particle agglomeration phenomenon of die face, it is characterised in that:
The fervent station of die face is equipped with earnestly cover, and the tangential direction for earnestly covering bottom is equipped with the air inlet and air outlet of word connection,
Air inlet connects wind turbine by ripple ajutage, and wind turbine is with the centrifugal fan for adjusting air-supply swivelling cover, and wind turbine is sent
Air port is higher than the 160 ~ 200mm of air inlet earnestly covered, and the air outlet earnestly covered then connects air-cooled feeding passage.
7. the method according to claim 5 for solving the fervent high-viscosity material particle agglomeration phenomenon of die face, it is characterised in that:
The circulating cooling system includes the first sedimentation basin, the second sedimentation basin, cooling column, cistern;First sedimentation basin receives lubrication water
The water that sub-sieve laminar flow goes out, the second sedimentation basin are connected to by pipeline between the first sedimentation basin and cooling column, cooling column cooling treatment
Water afterwards is stored in cistern, and cistern connects water inlet pipe by water pump, and water inlet pipe is equipped with control water valve.
8. the method for the fervent high-viscosity material particle agglomeration phenomenon of solution die face according to claim 3 or 6, feature exist
In:The fervent station of die face is equipped with the anti-blade on knife rest, and knife rest connects the output shaft of fervent motor.
Priority Applications (1)
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CN201711426413.6A CN108162234A (en) | 2017-12-26 | 2017-12-26 | The method for solving the fervent high-viscosity material particle agglomeration phenomenon of die face |
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CN201711426413.6A CN108162234A (en) | 2017-12-26 | 2017-12-26 | The method for solving the fervent high-viscosity material particle agglomeration phenomenon of die face |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111055470A (en) * | 2019-11-19 | 2020-04-24 | 广东华新电缆实业有限公司 | Production method of cable outer sheath |
CN114953245A (en) * | 2022-04-22 | 2022-08-30 | 东莞市杰夫阻燃材料有限公司 | Cooling forming process for flame-retardant master batch |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202462696U (en) * | 2011-12-30 | 2012-10-03 | 广东联塑机器制造有限公司 | Water-cooled granulating air tank and granulating production system |
CN204773123U (en) * | 2015-06-24 | 2015-11-18 | 惠州市金浩润电业有限公司 | Micelle cooling device |
CN205462789U (en) * | 2015-12-31 | 2016-08-17 | 江苏博迁新材料有限公司 | High -speed water conservancy diversion cyclone is broken up and is exported grader |
CN205613594U (en) * | 2016-05-12 | 2016-10-05 | 神华集团有限责任公司 | Cyclone and polyolefin production system |
-
2017
- 2017-12-26 CN CN201711426413.6A patent/CN108162234A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202462696U (en) * | 2011-12-30 | 2012-10-03 | 广东联塑机器制造有限公司 | Water-cooled granulating air tank and granulating production system |
CN204773123U (en) * | 2015-06-24 | 2015-11-18 | 惠州市金浩润电业有限公司 | Micelle cooling device |
CN205462789U (en) * | 2015-12-31 | 2016-08-17 | 江苏博迁新材料有限公司 | High -speed water conservancy diversion cyclone is broken up and is exported grader |
CN205613594U (en) * | 2016-05-12 | 2016-10-05 | 神华集团有限责任公司 | Cyclone and polyolefin production system |
Non-Patent Citations (3)
Title |
---|
中国轻工总会: "《轻工业技术装备手册》", 31 March 1996, 机械工业出版社 * |
孔萍等: "《塑料配混技术》", 31 August 2009, 中国轻工业出版社 * |
耿孝正: "《塑料机械的使用与维护》", 31 August 1998, 中国轻工业出版社 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111055470A (en) * | 2019-11-19 | 2020-04-24 | 广东华新电缆实业有限公司 | Production method of cable outer sheath |
CN114953245A (en) * | 2022-04-22 | 2022-08-30 | 东莞市杰夫阻燃材料有限公司 | Cooling forming process for flame-retardant master batch |
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Application publication date: 20180615 |