CN1377766A - Method for single layer or multilayer coextruding two-way extension polypropylene film and special equipment - Google Patents
Method for single layer or multilayer coextruding two-way extension polypropylene film and special equipment Download PDFInfo
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- CN1377766A CN1377766A CN 02112777 CN02112777A CN1377766A CN 1377766 A CN1377766 A CN 1377766A CN 02112777 CN02112777 CN 02112777 CN 02112777 A CN02112777 A CN 02112777A CN 1377766 A CN1377766 A CN 1377766A
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- 239000004743 Polypropylene Substances 0.000 title claims abstract description 27
- -1 polypropylene Polymers 0.000 title claims abstract description 27
- 229920001155 polypropylene Polymers 0.000 title claims abstract description 27
- 238000000034 method Methods 0.000 title claims description 31
- 239000002356 single layer Substances 0.000 title 1
- 238000001816 cooling Methods 0.000 claims abstract description 52
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- 238000007493 shaping process Methods 0.000 claims description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000003851 corona treatment Methods 0.000 claims description 8
- 238000005096 rolling process Methods 0.000 claims description 8
- 238000001125 extrusion Methods 0.000 claims description 5
- 238000005057 refrigeration Methods 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 239000000463 material Substances 0.000 abstract description 7
- 238000005520 cutting process Methods 0.000 abstract description 3
- 230000007246 mechanism Effects 0.000 abstract description 3
- 238000004804 winding Methods 0.000 abstract 2
- 229920006379 extruded polypropylene Polymers 0.000 abstract 1
- 230000000087 stabilizing effect Effects 0.000 abstract 1
- 238000007789 sealing Methods 0.000 description 14
- 230000008569 process Effects 0.000 description 4
- 230000002457 bidirectional effect Effects 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 229920006280 packaging film Polymers 0.000 description 3
- 239000012785 packaging film Substances 0.000 description 3
- 206010009866 Cold sweat Diseases 0.000 description 2
- 241000282326 Felis catus Species 0.000 description 2
- 229920006378 biaxially oriented polypropylene Polymers 0.000 description 2
- 239000011127 biaxially oriented polypropylene Substances 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000012775 heat-sealing material Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000010791 quenching Methods 0.000 description 2
- 229920006300 shrink film Polymers 0.000 description 2
- 230000001360 synchronised effect Effects 0.000 description 2
- 239000002390 adhesive tape Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010892 electric spark Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
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- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Abstract
During the production of two-way extended polypropylene film, the tube extruder extruded polypropylene tube blank is cooled, set in a preheating extending tower and a high temperature setting tower, and wound in a winding system. The special equipment includes blank tube extruder, preheating extending tower, and corona film edge cutting and winding system as well as high temperature setting tower comprising film bubble stabilizing A-shaped plates, heating mechanism and cooling mechanism. The present invention makes it possible to make both single-layered film and multi-layered film, especially superlow temperature blast material with high quality, no surface damage and good longitudinal performance.
Description
One, technical field
The present invention relates to a kind of manufacture method and special equipment thereof of polypropylene film, particularly a kind of usefulness three bubble pipes carry out the method and the special equipment thereof of single or multiple lift coextruding two-way extension polypropylene film.
Two, background technology
Existing single or multiple lift coextruding two-way extension polypropylene film (thermal finalization is called for short the BOPP film) has three kinds of manufacture methods and corresponding special equipment; Flat film is pulling method, flat film synchro-draw method and gun tube pulling method one by one.
1, the flat film problem that exists of pulling method one by one:
1) flat film one by one the pulling method apparatus and process adopt earlier vertically back cross directional stretch, the horizontal physical property of the product of being produced is better than vertical performance, and any packaging film all is the vertical physical property of requirement on serviceability.
2) this equipment longitudinal stretching adopts contact, and utilization sheet roller preheats and the number difference of roller and roller stretches to sheet, because sheet and roller rotating speed can not be synchronous fully, so roller can scratch film surface to some extent.
3) contact preheating sheet and vertically contact stretching mode, limited the use of three-layer co-extruded top layer heat-sealable material, more can not use the heat-sealable material (heat-sealable material that is clamminess below 105 degree) of ultralow temperature, thereby limit the development of heat-sealing film to high-speed packaging, low-temperature heat-sealing direction.
2, flat film synchro-draw method (synchronous motor or mechanical type) existing problems:
1) investment of main equipment and auxiliary equipment is big, and gross investment reaches RMB more than 400,000,000, and input-output ratio is science, unreasonable not, the production cost height, and be not easy to produce multi-assortment production, occupation area of equipment is big.
2) though product quality is fine, the vertical rerum natura of film might as well be adjusted, and production energy consumption height has restricted market application and development that flat film synchro-draw method device systems is produced the Biaxially oriented polypropylene packaging film.
3, the problem of bubble pipe pulling method existence:
1) present individual layer list bubble pipe lower blowing method only can be produced down and blow small-bore polypropylene packaging film (vertically and horizontally stretching is than about ten times).
2) blowing two bubble pipe pulling methods under the present domestic polypropylene only can produce down and blow polypropylene and do not have thermal finalization shrink wrap (no high-temperature shaping shrinkage factor is uncontrollable).
3) the two bubble of state-of-the-art in the world at present employing pipe method is produced the bidirectional stretching polypropylene film product (heat setting) with the identical performance of flat embrane method (stretching and synchro-draw one by one), be to use two kinds of modular systems and use corresponding technology and just can finish: a) non-heat-sealing type film adopts the heating plate contact to finalize the design and controls the film shrinkage factor, if will realize heat sealability, must make film enter another set of low temperature coating equipment and carry out the coating of low-temperature heat-sealing material; B) the heat-sealing type film adopts contactlessly, clips film by clip and passes through in hot-air oven, control the shrinkage factor of film with high-temperature shaping, but this equipment can not use the ultra-low temperature heat sealing material equally, as the heat-sealable material below 105 ℃.Produce many kinds (non-heat-sealing type, heat-sealing type, ultra-low temperature heat sealing type) bidirectional stretching polypropylene film that performance is identical under wanting to accomplish at same set of device systems, with a kind of process conditions, at present international and domestic also beyond example.
Three, summary of the invention
1, goal of the invention: the objective of the invention is a kind of individual layer, the plural layers can produced that propose, can produce the manufacture method and the special equipment thereof of the bidirectional stretching polypropylene film of non-heat-sealing type, heat-sealing type, ultra-low temperature heat sealing type film again in order to solve the defective that above three kinds of distinct devices and production technology exist.
2, technical scheme: for achieving the above object, the method for single or multiple lift coextruding two-way extension polypropylene film of the present invention the steps include:
1) extrudes annular single or multiple lift polypropylene embryonic tube through the machine head port mould of extruder, feed refrigerating gas through the inner cool tube road of automatic pressure control valve and carry out interior cooling, carry out outer cooling by kind of refrigeration cycle water, make embryonic tube enter further cooling in the tank by clamping carry-over pinch rolls then;
2) by pinch roll V1 embryonic tube is pulled out tank, dewater by the compressed air air knife, under the traction of pinch roll V1, enter the preheat stretch tower that comprises contactless preheating zone, drawing zone and cooling zone, in the preheat stretch tower,, realize cross directional stretch by certain air pressure blown film bubble to the suitable compressed air of the inner adding of film bubble, while is under the traction of pinch roll V2, and the speed difference between pinch roll V1, V2 realizes longitudinal stretching about passing through;
3) carry out the air cooling to finishing in length and breadth to the film that stretches, mechanical traction by pinch roll V3, send into the high-temperature shaping tower that comprises high-temperature shaping district and cooling zone, under the situation of pinch roll V3 and pinch roll V4 speed basic synchronization, in the film bubble, inject the compressed air of certain pressure, realize high-temperature shaping and cooling and shaping;
4) according to the client to the requirement of product width and needs sided corona treatment whether, divides and cuts open and sided corona treatment, enter the rolling system then and finish rolling, the formation final products.
Wherein: 1), the temperature of refrigerating gas is a subzero, and the temperature of cooling circulating water is 12-30 ℃;
2) in, the length of preheating zone is 5-6.5m, adopts the far infrared preheating method, and preheat temperature is 180-250 ℃, and the length of drawing zone is 6-7m, and temperature is 140-210 ℃, the length of cooling zone is 7-8m, adopts 15-30 ℃ cooling air;
3) in, the length in high-temperature shaping district is 4-5m, and temperature is 150-220 ℃, and the length of cooling zone is 6-8m, adopts 15-30 ℃ cooling air.
The equipment of single or multiple lift coextruding two-way extension polypropylene film of the present invention, comprise embryonic tube extrusion device, preheat stretch tower and film corona side cut wrap-up, it is characterized in that it also comprises the high-temperature shaping tower, this high-temperature shaping tower is made up of the film bubble stabilizes letter stencil at two ends about being arranged on and heating arrangements and the cooling body that is arranged between the collapser, high-temperature shaping tower and preheat stretch tower are vertically mounted on the rack platform, and the high-temperature shaping tower is between preheat stretch tower and film corona side cut wrap-up.
Wherein: the heating arrangements in the described high-temperature shaping tower is made of far-infrared heater.
Cooling body in the described high-temperature shaping tower forces cooling tube and contact water flowing chill roll to constitute by contactless cooling air, contactless cooling air forces cooling tube to place the below of heating arrangements, and contact water flowing chill roll is positioned at the top of the film bubble stabilizes letter stencil of below.
3, beneficial effect: the present invention compared with prior art, its remarkable advantage is:
1) the present invention compares with pulling method one by one and has overcome the problem that the sheet preheating of contact thickness and longitudinal stretching scratch film surface, and the more heat-sealable material of low temperature can be used in the top layer of film simultaneously, the desirable heat-sealable material that is clamminess as 85 ° of degree.
2) improved the low-temperature heat-sealing planarization, improved bag speed and heat seal strength and sealed presentation quality.
3) solved the following temperature bag of film thermal change type, breakthrough polypropylene (ring-like) the thermal contractive label film that solved substitutes polyvinyl chloride shrink label film; solved VCM environmental pollution problem; also alternative paper label; problems such as papermaking resource problem and mechanical packaging operation instead of manual pasted paper label have been solved simultaneously; thereby enlarged the use field of this product, made contribution for protecting forest resources, protect environment.
4) solve the polypropylene symmetry problem of intermolecular arrangement when stretching in length and breadth, thereby solved vertical Young's modulus of film and lateral balance problem.
Four, description of drawings
Accompanying drawing is the structural representation of special equipment of the present invention.
Wherein: the 1-main extruder; The 2-head; The 3-water quench tank; The 4-guide roller; 5-embryonic tube moisture drying system; Preheating of 6-embryonic tube and bi-directional synchronization drawing zone; 7, the contactless cooling air of 12-is forced cooling tube; 8,13-contact water flowing chill roll; 9,10,14-film bubble stabilizes letter stencil; 11-Far-infrared Heating high-temperature shaping district; 15-film corona side cut rolling system; V1, V2, V3, V4-clamp carry-over pinch rolls; The 16-embryonic tube; The 17-film.
Five, the specific embodiment
Film-forming method and special equipment that present embodiment adopts, can process following polypropylene film:
The heat-sealing film class: cigarette pack film, candy wrapping film, pearly-lustre film, loop tag shrink film, in length and breadth to shrinkage ratio greater than 50% bridging type heat-sealing shrink film.
Non-heat-sealing film class: print film, mould/mould composite membrane, paper/mould composite membrane, adhesive tape film etc.
The fabric width of product is that 1100mm, output are 1000 tons/year.
The processing step of system film is:
1) main extruder plasticizing HOPP, plasticization temperature is 220-280 ℃; Assist extruder A/C plasticizing COPP, plasticization temperature is 210-280 ℃, and main extruder reaches the melt pipe that passes through separately by planet filter, subsidiary engine by the superposing type filter and imports the flexible self-regulated annular of inner-cooled head.
2) be extruded into the annular polypropylene embryonic tube of thickness 1.5-2mm through machine head port mould, the refrigerating gas that feeds-50 ℃ through the inner cool tube road of automatic pressure control valve cools off, external cooling passes through 12-30 ℃ refrigeration cool cycles water cooling, and embryonic tube enters further cooling in the tank by clamping carry-over pinch rolls.
3) embryonic tube pulls out tank by pinch roll V1, dewater by the compressed air air knife, enter pinch roll V1, send into the long contactless far infrared sheet preheating zone (temperature: 180-250 ℃) of 5-6.5m, enter long drawing zone (temperature: 140-210 ℃) of 6-7m and the long cooling zone (15-30 ℃ of cooling air) of 7-8m again, enter pinch roll V2 again, the suitable compressed air of the inner adding of film bubble simultaneously, realize cross directional stretch by certain air pressure inflation, under given mechanical traction power, the speed difference that produces by pinch roll V1 and pinch roll V2 realizes longitudinal stretching simultaneously.
4) carry out the air cooling to finishing in length and breadth to the film that stretches, mechanical traction by pinch roll V3, send into long high-temperature shaping district (temperature: 150-220 ℃) of 4-5m and the long cooling zone (15-30 ℃ of cooling air) of 6-8m, under the situation of pinch roll V3 and pinch roll V4 speed basic synchronization, inject the compressed air of certain pressure, realize high-temperature shaping and cooling and shaping.
5) according to the client to the requirement of product width and needs sided corona treatment whether, divide and cut open and sided corona treatment.Through winder mechanical traction, film impacts the realization sided corona treatment through the electric spark of 4 kilowatts of high pressure generators, realize that through vertical cutting knife of cutting roller and can laterally adjust of trough of belt cuing open the limit cuts again, enter the two rolling systems of rotary centre-driven double then and finish rolling, form final products.
The special equipment of system film comprises extrusion device, preheat stretch tower, high-temperature shaping tower and film corona side cut wrap-up.
Extrusion device comprises 1 of main extruder, satellite-type extruder 2, three layers composite machine head, calibration sleeve and water quench tank.
The preheat stretch tower begins to set gradually guide roller, embryonic tube moisture baking zone, V1 clamping carry-over pinch rolls, embryonic tube preheating and bi-directional synchronization drawing zone, contactless cooling air pressure cooling tube, contact water flowing chill roll, film bubble stabilizes letter stencil and V2 from cat head and clamps carry-over pinch rolls.
The high-temperature shaping tower begins to be disposed with V3 from cat head and clamps carry-over pinch rolls, film bubble stabilizes letter stencil, Far-infrared Heating fortune type mechanism, contactless cooling air pressure cooling tube, contact water flowing chill roll, film bubble stabilizes letter stencil and V4 clamping carry-over pinch rolls.
Film corona side cut wrap-up comprises that two-sided corona treatment system, two slitter edge that cuts open reclaim two rolling systems that reach.
Preheat stretch tower and high-temperature shaping tower are fixed on the steelframe platform, and the installation site of each parts of entire equipment system determines by technological process.
Embryonic tube extrusion device, preheat stretch tower and film corona side cut wrap-up and existing relevant device are basic identical.
Claims (7)
1, a kind of method of single or multiple lift coextruding two-way extension polypropylene film is characterized in that it comprises the steps:
1) extrudes annular single or multiple lift polypropylene embryonic tube through the machine head port mould of extruder, feed refrigerating gas through the inner cool tube road of automatic pressure control valve and carry out interior cooling, carry out outer cooling by kind of refrigeration cycle water, make embryonic tube enter further cooling in the tank by clamping carry-over pinch rolls then;
2) by pinch roll V1 embryonic tube is pulled out tank, under the traction of pinch roll V1, enter the preheat stretch tower that comprises contactless preheating zone, drawing zone and cooling zone, in the preheat stretch tower, to the suitable compressed air of the inner adding of film bubble, realize cross directional stretch by certain air pressure blown film bubble, the while is under the traction of pinch roll V2, and the speed difference between pinch roll V1, V2 realizes longitudinal stretching about passing through;
3) carry out the air cooling to finishing in length and breadth to the film that stretches, mechanical traction by pinch roll V3, send into the high-temperature shaping tower that comprises high-temperature shaping district and cooling zone, under the situation of pinch roll V3 and pinch roll V4 speed basic synchronization, in the film bubble, inject the compressed air of certain pressure, realize high-temperature shaping and cooling and shaping;
4) according to the client to the requirement of product width and needs sided corona treatment whether, divides and cuts open and sided corona treatment, enter the rolling system then and finish rolling, the formation final products.
2, the method for single or multiple lift coextruding two-way extension polypropylene film according to claim 1 is characterized in that in step 1, and the temperature of refrigerating gas is a subzero, and the temperature of cooling circulating water is 12-30 ℃.
3, the method for single or multiple lift coextruding two-way extension polypropylene film according to claim 1, it is characterized in that in step 2, the length of preheating zone is 5-6.5m, adopt the far infrared preheating method, preheat temperature is 180-250 ℃, and the length of drawing zone is 6-7m, and temperature is 140-210 ℃, the length of cooling zone is 7-8m, adopts 15-30 ℃ cooling air.
4, the method for single or multiple lift coextruding two-way extension polypropylene film according to claim 1, it is characterized in that in step 3 length in high-temperature shaping district is 4-5m, temperature is 150-220 ℃, the length of cooling zone is 6-8m, adopts 15-30 ℃ cooling air.
5, a kind of special equipment of single or multiple lift coextruding two-way extension polypropylene film, comprise embryonic tube extrusion device, preheat stretch tower and film corona side cut wrap-up, it is characterized in that it also comprises the high-temperature shaping tower, this high-temperature shaping tower is made up of the film bubble stabilizes letter stencil at two ends about being arranged on and heating arrangements and the cooling body that is arranged between the collapser, high-temperature shaping tower and preheat stretch tower are vertically mounted on the rack platform, and the high-temperature shaping tower is between preheat stretch tower and film corona side cut wrap-up.
6, the special equipment of single or multiple lift coextruding two-way extension polypropylene film according to claim 5 is characterized in that the heating arrangements in the described high-temperature shaping tower is made of far-infrared heater.
7, the special equipment of single or multiple lift coextruding two-way extension polypropylene film according to claim 5, it is characterized in that the cooling body in the described high-temperature shaping tower is made of contactless cooling air pressure cooling tube and contact water flowing chill roll, contactless cooling air forces cooling tube to place the below of heating arrangements, and contact water flowing chill roll is positioned at the top of below film bubble stabilizes letter stencil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021127778A CN1160182C (en) | 2002-03-19 | 2002-03-19 | Method for single layer or multilayer coextruding two-way extension polypropylene film and special equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021127778A CN1160182C (en) | 2002-03-19 | 2002-03-19 | Method for single layer or multilayer coextruding two-way extension polypropylene film and special equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1377766A true CN1377766A (en) | 2002-11-06 |
| CN1160182C CN1160182C (en) | 2004-08-04 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021127778A Expired - Fee Related CN1160182C (en) | 2002-03-19 | 2002-03-19 | Method for single layer or multilayer coextruding two-way extension polypropylene film and special equipment |
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| Country | Link |
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| CN (1) | CN1160182C (en) |
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1311960C (en) * | 2004-02-26 | 2007-04-25 | 甘国工 | Method and device of continuous producing orthogonal complex bidirection antistretching cylindrical film having heat-seal lager |
| CN100355554C (en) * | 2004-10-13 | 2007-12-19 | 甘国工 | Continuous method for fabricating orthogonal composite bidirectional tensile cylindrical shaped membrane with heat seal layer, and equipment |
| WO2009135341A1 (en) * | 2008-05-04 | 2009-11-12 | Yang Chi-Tsan | A method of making a shrinkable plastic film by environment-friendly resin materials |
| WO2009143663A1 (en) * | 2008-05-28 | 2009-12-03 | Yang Chi-Tsan | An improved processs and apparatus for producing a shrinkable plastic film by environment-friendly resin material |
| CN101879805A (en) * | 2010-06-01 | 2010-11-10 | 中山博锐斯塑胶新材料有限公司 | Multilayer film production equipment and multilayer film production method |
| CN101290358B (en) * | 2007-04-20 | 2011-07-13 | 富士胶片株式会社 | Thermal processing method for thermoplastic film, thermoplastic film and method for making same |
| CN102700121A (en) * | 2012-06-11 | 2012-10-03 | 江苏苏力机械有限公司 | Heating and heat preservation device for ultra-wide film synchronous stretching machine |
| CN103192523A (en) * | 2012-01-06 | 2013-07-10 | 上海通冷包装材料有限公司 | Heat-shrinkable PVC film unit |
| CN103213233A (en) * | 2013-04-16 | 2013-07-24 | 中山博锐斯塑胶新材料有限公司 | TPU (Thermoplastic Polyurethane) hot melt adhesive membrane production device |
| CN103707528A (en) * | 2013-12-31 | 2014-04-09 | 青岛顺德塑料机械有限公司 | High-permeability membrane production line and high-permeability membrane production process |
| CN104015349A (en) * | 2014-06-10 | 2014-09-03 | 四川大学 | Online thermal control device and method of PLA (polylactic acid) blown film |
| CN105196524A (en) * | 2015-10-08 | 2015-12-30 | 杭州和顺科技股份有限公司 | Preparation method of blue double-direction stretching type polyester film |
| CN105946211A (en) * | 2016-06-23 | 2016-09-21 | 浙江汇锋薄膜科技有限公司 | Improved PVC membrane blowing machine |
| CN109093997A (en) * | 2018-10-25 | 2018-12-28 | 刘宝龙 | A kind of continous way vertically and horizontally film stretching apparatus |
| CN109367046A (en) * | 2018-09-26 | 2019-02-22 | 江阴长庚高科技材料有限公司 | A kind of high-impact two-way stretching polyamide film and thirdly bubble production method and application |
| CN110922683A (en) * | 2019-11-15 | 2020-03-27 | 安徽国风塑业股份有限公司 | Thick BOPP film and preparation method thereof |
| CN112123746A (en) * | 2020-08-14 | 2020-12-25 | 广东金明精机股份有限公司 | Apparatus and method for subsequent foaming of film |
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2002
- 2002-03-19 CN CNB021127778A patent/CN1160182C/en not_active Expired - Fee Related
Cited By (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1311960C (en) * | 2004-02-26 | 2007-04-25 | 甘国工 | Method and device of continuous producing orthogonal complex bidirection antistretching cylindrical film having heat-seal lager |
| CN100355554C (en) * | 2004-10-13 | 2007-12-19 | 甘国工 | Continuous method for fabricating orthogonal composite bidirectional tensile cylindrical shaped membrane with heat seal layer, and equipment |
| CN101290358B (en) * | 2007-04-20 | 2011-07-13 | 富士胶片株式会社 | Thermal processing method for thermoplastic film, thermoplastic film and method for making same |
| WO2009135341A1 (en) * | 2008-05-04 | 2009-11-12 | Yang Chi-Tsan | A method of making a shrinkable plastic film by environment-friendly resin materials |
| WO2009143663A1 (en) * | 2008-05-28 | 2009-12-03 | Yang Chi-Tsan | An improved processs and apparatus for producing a shrinkable plastic film by environment-friendly resin material |
| CN101590694B (en) * | 2008-05-28 | 2011-07-27 | 杨启赞 | Device and improved method for preparing contracting glue film by environmental-friendly material and device thereof |
| CN101879805A (en) * | 2010-06-01 | 2010-11-10 | 中山博锐斯塑胶新材料有限公司 | Multilayer film production equipment and multilayer film production method |
| CN101879805B (en) * | 2010-06-01 | 2012-10-17 | 中山博锐斯塑胶新材料有限公司 | Multilayer film production equipment and multilayer film production method |
| CN103192523A (en) * | 2012-01-06 | 2013-07-10 | 上海通冷包装材料有限公司 | Heat-shrinkable PVC film unit |
| CN102700121A (en) * | 2012-06-11 | 2012-10-03 | 江苏苏力机械有限公司 | Heating and heat preservation device for ultra-wide film synchronous stretching machine |
| CN103213233A (en) * | 2013-04-16 | 2013-07-24 | 中山博锐斯塑胶新材料有限公司 | TPU (Thermoplastic Polyurethane) hot melt adhesive membrane production device |
| CN103707528A (en) * | 2013-12-31 | 2014-04-09 | 青岛顺德塑料机械有限公司 | High-permeability membrane production line and high-permeability membrane production process |
| CN103707528B (en) * | 2013-12-31 | 2016-11-16 | 青岛顺德塑料机械有限公司 | A kind of high transmittance film production line and production technology thereof |
| CN104015349A (en) * | 2014-06-10 | 2014-09-03 | 四川大学 | Online thermal control device and method of PLA (polylactic acid) blown film |
| CN105196524A (en) * | 2015-10-08 | 2015-12-30 | 杭州和顺科技股份有限公司 | Preparation method of blue double-direction stretching type polyester film |
| CN105946211A (en) * | 2016-06-23 | 2016-09-21 | 浙江汇锋薄膜科技有限公司 | Improved PVC membrane blowing machine |
| CN109367046A (en) * | 2018-09-26 | 2019-02-22 | 江阴长庚高科技材料有限公司 | A kind of high-impact two-way stretching polyamide film and thirdly bubble production method and application |
| CN109367046B (en) * | 2018-09-26 | 2021-10-29 | 江阴长庚高科技材料有限公司 | High-impact-resistance biaxially oriented polyamide film and three-bubble production method and application thereof |
| CN109093997A (en) * | 2018-10-25 | 2018-12-28 | 刘宝龙 | A kind of continous way vertically and horizontally film stretching apparatus |
| CN109093997B (en) * | 2018-10-25 | 2021-03-09 | 刘宝龙 | Continuous longitudinal and transverse film stretching equipment |
| CN110922683A (en) * | 2019-11-15 | 2020-03-27 | 安徽国风塑业股份有限公司 | Thick BOPP film and preparation method thereof |
| CN112123746A (en) * | 2020-08-14 | 2020-12-25 | 广东金明精机股份有限公司 | Apparatus and method for subsequent foaming of film |
| CN112123746B (en) * | 2020-08-14 | 2021-07-06 | 广东金明精机股份有限公司 | Apparatus and method for subsequent foaming of film |
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| CN1160182C (en) | 2004-08-04 |
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