CN106182836A - Polymer composite paper production equipment - Google Patents
Polymer composite paper production equipment Download PDFInfo
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- CN106182836A CN106182836A CN201610747393.1A CN201610747393A CN106182836A CN 106182836 A CN106182836 A CN 106182836A CN 201610747393 A CN201610747393 A CN 201610747393A CN 106182836 A CN106182836 A CN 106182836A
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- screw
- polymer
- mixing
- spiral shell
- melt
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29D—PRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
- B29D7/00—Producing flat articles, e.g. films or sheets
- B29D7/01—Films or sheets
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- 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
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C31/00—Handling, e.g. feeding of the material to be shaped, storage of plastics material before moulding; Automation, i.e. automated handling lines in plastics processing plants, e.g. using manipulators or robots
- B29C31/04—Feeding of the material to be moulded, e.g. into a mould cavity
- B29C31/06—Feeding of the material to be moulded, e.g. into a mould cavity in measured doses, e.g. by weighting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/02—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of definite length, i.e. discrete articles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/288—Feeding the extrusion material to the extruder in solid form, e.g. powder or granules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/402—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders the screws having intermeshing parts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2007/00—Flat articles, e.g. films or sheets
- B29L2007/002—Panels; Plates; Sheets
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Robotics (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The invention provides a polymer composite paper production device, which comprises a raw material supply system, a mixed feeding system, a double-screw mixing and granulating system, a finished product particle packaging system, a double-screw mixing and extruding system, a sheet forming and extruding system and a sheet forming auxiliary machine system, wherein the raw material supply system is connected with the double-screw mixing and granulating system; the equipment does not discharge three wastes in the production process, and simultaneously, the equipment cost is only one tenth of the cost of the traditional paper production equipment, and the occupied plant area is small.
Description
Technical field
The present invention relates to a kind of production equipment, in particular it relates to a kind of polymer is combined paper producing apparatus.
Background technology
Traditional paper mainly possesses following shortcoming: raw material needs timber and natural plant fibre, greatly
Amount is destroyed the forest reserves and causes environmental pollution.Whole production process needs use substantial amounts of water, simultaneously need to add strong acid, strong
Alkali, bleaching powder and numerous organic chloride, exist steaming and decocting, wash, several important pollution sections such as bleaching, produce " three wastes " and make
The pollution problem become.Traditional paper complete set of equipments price is high, floor space is huge, and early stage needs to spend ample resources to buy and sets
Standby and build Factory Building.
For the above-mentioned major defect of traditional paper, my company develops " a kind of polymer extrusion coating paper complete production unit ",
This complete set of equipments is used for producing polymer extrusion coating paper.This extrusion coating paper is raw material without Fiber Materials such as timber, and production process is without " three
Useless " discharge, equipment cost is only 1/10th of traditional paper simultaneously, and shared plant area is the least.
Polymer extrusion coating paper is with synthetic resin such as polystyrene, polypropylene, polyethylene as primary raw material.Produce according to final
Performance required by product, it is often various polymer, inorganic powder and other organic combination products." making of extrusion coating paper
Paper " process, the actually process of synthetic resin casting film-forming, the feature of the tape casting is die head extruded velocity and casting roller
There is bigger speed difference in linear velocity, by regulating the speed, difference controls produced extrusion coating paper thickness, can produce
The synthetic paper of various different-thickness.
Summary of the invention
The present invention is to solve drawbacks described above and deficiency present in prior art, it is provided that a kind of polymer extrusion coating paper is raw
Product equipment.
For solving above-mentioned technical problem, the present invention provides a kind of polymer to be combined paper producing apparatus, including raw material supply is
System, mixing feed system, twin-screw mixer granulating system, finished particle packaging system, twin-screw mixer extrusion system, sheet material become
Type extrusion system and sheet forming auxiliary system；
Raw material feed system be used for the storage of raw material, conveying, quantitative weighing, then in individual ratio by feedstock transportation to mixing feeding
System；Mixing feed system is used for the bulk melt heated by each raw material, mixing is the most homogeneous, and feeds double spiral shell by drawing-in device
Bar mixing granulator system；Twin-screw mixer granulating system is for dissipating further for polymer melt compounding ingredients fully, being distributed all
Even melt, is made as solid particle of uniform size by pelletize and cooling device by melt；Finished particle packaging system is used
In solid particle being stored and packing, in case twin-screw mixer extrusion system uses；Twin-screw mixer extrusion system is by solid
Grain is melted and the degree of depth is mixing, mixing after melt enter sheet forming extrusion system；Polymer is melted by sheet forming extrusion system
Extrude to sheet forming auxiliary system from mould after body filtration, metering；Polymer melt is shaped also by sheet forming auxiliary system
It is cooled to polymer extrusion coating paper in uniform thickness, cuts rear rolling.
Further, described raw material feed system includes that material negative pressure conveying device, fluid Supplying apparatus and automatic ration claim
Refitting is put；Described material negative pressure conveying device is all connected with described automatic ration weighing device with described fluid Supplying apparatus；
Described material negative pressure conveying device includes that roots blower, material is defeated equipped with pulp-collecting box, the batch turning station of screw conveying device
Sending pipeline, operated pneumatic valve and Split filter device, described screw conveying device is driven by roots blower and is passed through by the raw material of pulp-collecting box
Material pipeline road flows to automatic ration weighing device, and described operated pneumatic valve arranges on Material pipeline road, powder body filter
The end on Material pipeline road, described powder body filter built-in cloth-bag type cartridge filter are set；
Described fluid Supplying apparatus includes liquid material head tank and liquid conveying oil pump；
Described automatic ration weighing device includes powder body gravimetric tank, liquid weighing tank and quantitative weighing sensing device, described powder body
Gravimetric tank top is provided with air filtration exhaust apparatus, and the top of described liquid weighing tank is provided with feeding mouth, and described feeding mouth passes through
Fluid pipeline is connected with fluid Supplying apparatus.
Further, described mixing feed system includes high-speed mixer and taper forced feed machine；Described high-speed mixer
Including pneumatic pot cover, the ladle body of sandwich, belt gear and pneumatic type discharging device, described pot cover is provided with observation
Mouth, charge door and air vent；Deflector and stirrer paddle it is provided with in described ladle body；Described taper forced feed machine includes transmission electricity
Machine, reduction box, twin screw intermeshing screw, tapered cylinder and feed box, be configured with forever below described tapered cylinder and feed box
Admittedly heat the heating rod of conduction oil.
Further, described twin-screw mixer granulating system include main motor one, parallel triple axle high torque reduction box one,
Screw rod one, machine barrel one and water ring pelletize subsidiary engine；
The output shaft of described main motor one is connected with the power shaft of reduction box one by shaft coupling, and described screw rod one is provided with spiral shell
Bar assembly；
Described screw arbor assembly includes carrying spiral shell block, mixing spiral shell block, mediating spiral shell block, damping block and derotation spiral shell block, and described screw rod one is
Screw arbor assembly arranged in series combines, described machine barrel one by 8 ~ 15 joint cylinders be composed in series, often joint cylinder for include housing and
Liner, the built-in cyclic water channel of described housing, outside is provided with electric heater；
Described water ring pelletize subsidiary engine include the fervent head of water ring die face, Water ring granulator, Water-circulating thermal cutting cover, water pump, water tank and from
Heart dewaterer forms；The described fervent head of water ring die face is made up of spreader and fervent die face, and Water ring granulator connection of getting home is cut
Grain blade, by spring level pressure blade on knife rest, patch floats in head die face, completes pelletizing action by rotation.
Further, described finished particle includes that system includes being dried ebullated bed, homogenization silo and automatic packaging machine, and material exists
It is dried on ebullated bed after carrying out dried and enters homogenization silo, then by automatic packaging machine, finished particle is packed.
Further, described twin-screw mixer extrusion system includes feeding machine, main motor two, reduction box two, screw rod two, machine
Cylinder two and exhaust apparatus；Described feeding machine includes feeding motor, feeding reduction box, feed screw, feeding machine barrel and hopper；Described
The output shaft of main motor two is connected with the power shaft of reduction box two by shaft coupling, and described screw rod two is provided with screw arbor assembly；
Described screw arbor assembly includes carrying spiral shell block, mixing spiral shell block, mediating spiral shell block, damping block and derotation spiral shell block, and described screw rod two is screw rod
Assembly arranged in series combines, and described machine barrel two is composed in series by 8 ~ 15 joint cylinders, and often joint cylinder is for including housing and liner,
The built-in cyclic water channel of described housing, outside is provided with electric heater.
Further, described sheet forming extrusion system includes double plunger type net-changing device, Melt Pump, sheet die；Institute
Stating net-changing device and be provided with oval flow distribution plate, described flow distribution plate is provided with metal screen；Runner it is provided with, stream in described sheet die
End, road is discharging opening, and the die lip of discharging opening is provided with regulation bolt and baffle plate, for regulating thickness and the width of lamellar melt.
Further, described sheet forming auxiliary system includes that calender, traction cooling bracket, edge-cutting device and double are received
Volume machine, the calendering of lamellar melt cooling and shaping that sheet die is extruded by calender are finished sheet, are then cooled down by traction
Sheet material is cooled down and carries by bracket；Sheet edge is cut to the wide cut of requirement and reclaims by edge-cutting device；Double rolling
Machine is for by final finished sheet rolling.
The Advantageous Effects that the present invention is reached: a kind of polymer that the present invention provides is combined paper producing apparatus, produces
During three-waste free discharge, simultaneously equipment cost be only traditional paper produce equipment cost 1/10th, shared plant area
Less, it includes raw material feed system, mixing feed system, twin-screw mixer granulating system, finished particle packaging system, double spiral shell
Bar mixing extrusion system, sheet forming extrusion system and sheet forming auxiliary system；Raw material feed system for raw material storage,
Conveying, quantitative weighing, then in individual ratio by feedstock transportation to mixing feed system；Mixing feed system is for adding each raw material
Heat, mixing are to homogeneous bulk melt, and feed twin-screw mixer granulating system by drawing-in device；Twin-screw mixer pelletize system
System, will be molten by pelletize and cooling device for the melt being dissipated fully by further for polymer melt compounding ingredients, being evenly distributed
System is as solid particle of uniform size；Finished particle packaging system is for storing solid particle and packing, in case double spiral shell
Bar mixing extrusion system uses；Twin-screw mixer extrusion system by mixing to solid particle melting the degree of depth, mixing after melt enter
Enter sheet forming extrusion system；Sheet forming extrusion system becomes after polymer melt filtration, metering to sheet material from mould extrusion
Type auxiliary system；Polymer melt is shaped and is cooled to polymer extrusion coating paper in uniform thickness by sheet forming auxiliary system, cuts out
Cut rear rolling.
Accompanying drawing explanation
Fig. 1-Fig. 3 present configuration schematic diagram.
Detailed description of the invention
The invention will be further described below in conjunction with the accompanying drawings.Following example are only used for clearly illustrating the present invention
Technical scheme, and can not limit the scope of the invention with this.
As Figure 1-3, the present invention provides a kind of polymer to be combined paper producing apparatus, including raw material feed system, mixing
Feed system, twin-screw mixer granulating system, finished particle packaging system, twin-screw mixer extrusion system, sheet forming are extruded
System and sheet forming auxiliary system；
Raw material feed system be used for the storage of raw material, conveying, quantitative weighing, then in individual ratio by feedstock transportation to mixing feeding
System；Mixing feed system is used for the bulk melt heated by each raw material, mixing is the most homogeneous, and feeds double spiral shell by drawing-in device
Bar mixing granulator system；Twin-screw mixer granulating system is for dissipating further for polymer melt compounding ingredients fully, being distributed all
Even melt, is made as solid particle of uniform size by pelletize and cooling device by melt；Finished particle packaging system is used
In solid particle being stored and packing, in case twin-screw mixer extrusion system uses；Twin-screw mixer extrusion system is by solid
Grain is melted and the degree of depth is mixing, mixing after melt enter sheet forming extrusion system；Polymer is melted by sheet forming extrusion system
Extrude to sheet forming auxiliary system from mould after body filtration, metering；Polymer melt is shaped also by sheet forming auxiliary system
It is cooled to polymer extrusion coating paper in uniform thickness, cuts rear rolling.
One, described raw material feed system includes material negative pressure conveying device 101, fluid Supplying apparatus 102 and automatic ration
Weighing device 103；Described material negative pressure conveying device 101 and described fluid Supplying apparatus 102 are all weighed with described automatic ration
Device 103 is connected；
Described material negative pressure conveying device 101 includes equipped with pulp-collecting box, the batch turning station of screw conveying device, roots blower, thing
Material conveying tube road, operated pneumatic valve and Split filter device, described screw conveying device is driven the raw material of pulp-collecting box by roots blower
Flowing to automatic ration weighing device by Material pipeline road, described operated pneumatic valve arranges on Material pipeline road, powder body mistake
Filter arranges the end on Material pipeline road, described powder body filter built-in cloth-bag type cartridge filter；Wherein, bolt conveyer device electricity
Acc power is 0.75-1.5KW, and roots blower power is 5.5-10.5KW, pipe diameter Ф=50 used by Material pipeline road ~
100mm, material is rustless steel
Described fluid Supplying apparatus 102 includes liquid material head tank and liquid conveying oil pump；Head tank volume 1 ~ 3m3, material is stainless
Steel, thickness δ=1 ~ 3mm, configuration level detector and manually-operated gate, liquid conveying oil pump power 0.75 ~ 1.5kw, maximum stream flow 3700L/
H；Liquid conducting pipes, material is rustless steel.
Described automatic ration weighing device 103 includes powder body gravimetric tank, liquid weighing tank and quantitative weighing sensing device, institute
Stating powder body gravimetric tank top and be provided with air filtration exhaust apparatus, the top of described liquid weighing tank is provided with feeding mouth, described pan feeding
Mouth is connected with fluid Supplying apparatus by fluid pipeline；Powder body gravimetric tank volume 1000 ~ 1500L, material rustless steel, thickness δ=2 ~
4mm, liquid weighing tank volume 30 ~ 80L, material rustless steel, thickness δ=2 ~ 4mm.
Two, described mixing feed system includes high-speed mixer 201 and taper forced feed machine 202；
Described high-speed mixer 201 includes that pot cover described in pneumatic pot cover is provided with observation panel, charge door and air vent, material 304
Weldment；The ladle body of sandwich, its internal layer is 304 weldments, and thickness 10mm inside ladle body added with deflector and material is
The stirrer paddle of 304 foundry goods, stirrer paddle quantity 2 ~ 4, interior ladle body total measurement (volume) 800 ~ 1500L；Belt gear, motor merit
Rate 150 ~ 250KW, rotating speed is by Frequency Converter Control；Pneumatic type discharging device, drain hole diameter 300mm；
Described taper forced feed machine 202 includes driving motor, driving motor power 7.5 ~ 11kw, frequency control；Reduction box,
Big output speed 11rpm；Twin screw intermeshing screw, counter rotating, tapering 22 °, outside diameter φ 393mm, end diameter φ
70mm；Tapered cylinder and feed box, be configured with the heating rod the most admittedly heating conduction oil below described tapered cylinder and feed box；
Three, described twin-screw mixer granulating system includes main motor 1, parallel triple axle high torque reduction box 1, spiral shell
Bar 303, machine barrel one and water ring pelletize subsidiary engine 304；
Main motor 1 uses alternating current generator or direct current generator, and rotating speed uses AC converter or DC speed regulator regulation, electricity
Motivation output shaft is connected with twin screw reduction box 1 power shaft by shaft coupling, motor power (output) 90 ~ 200KW；
Parallel triple axle high torque reduction box 1, gear ratio i=3 ~ 5, output speed 300 ~ 500RPM；
Described screw rod 1 is provided with screw arbor assembly；Described screw arbor assembly includes carrying spiral shell block, mixing spiral shell block, mediating spiral shell block, resistance
Buddhist nun's block and derotation spiral shell block, described screw rod is that screw arbor assembly arranged in series combines, and screw rod rotated versions is twin screw engagement type
Rotating Vortex, screw slenderness ratio L/D=36:1 ~ 48:1, outer screw diameter Φ=61.5 ~ 94.5mm, described machine barrel one is by 8 ~ 15 joint cylinders
Body is composed in series, machine barrel draw ratio L/D=36:1 ~ 48:1, and housing uses 45# steel to be base material, and built-in cyclic water channel is used for reducing cylinder
Temperature, outside parcel electric heater is for heating the material in machine barrel；Cylinder lining is that " ∞ " structure uses the resistance to break-in of high-quality
Golden and thermally treated, cylinder bore Φ=62 ~ 95mm.
Described water ring pelletize subsidiary engine 304 includes the fervent head of water ring die face, Water ring granulator, Water-circulating thermal cutting cover, water pump, water
Case and centrifugal dehydrator composition；The described fervent head of water ring die face is made up of spreader and fervent die face, and Water ring granulator is got home
Connecting pelletizing blade, by spring level pressure blade on knife rest, patch floats in head die face, completes pelletizing action by rotation.Water
Ring fervent cover material is rustless steel, thickness δ=10 ~ 20mm；Pump power 3 ~ 7.5KW, water tank material is rustless steel；Centrifuge dehydration
Machine shell and internal net-shaped drum material are rustless steel, and reducing motor drives, pulley drive, and reducing motor power 5.5 ~
11KW。
Four, described finished particle includes that system includes:
It is dried ebullated bed 401, cylinder volume 3000 ~ 4000L；Charge 1000 ~ 2500kg；Staving material: inner bag uses 2.0mm
Rustless steel makes, and shell 2mmA3 plate makes, and centre adds special insulation material；Dry heat power: 60KW, 15,4kw root；
Mode of heating: electric heater for heating；Dehumidifying casing 50*50*3mm；Power of fan: 5.5 ~ 7.5KW；Regeneration power of fan: 1.5 ~
2.2KW；Regeneration heating power: heating rod 6, power 18KW；
Homogenization silo 402, is made up of feed bin, pipeline and blower fan.Feed bin volume 8 ~ 10m；Power of fan 3 ~ 5.5KW, pipeline includes
Pipeline, threeway and elbow, diameter of phi 130 ~ 160mm；
Material enters homogenization silo after carrying out dried on dry ebullated bed, then by automatic packaging machine 403 to finished product
Granule is packed.
Five, described twin-screw mixer extrusion system includes feeding machine 501, main motor 2 502, reduction box 2 503, screw rod
2 504, machine barrel two and exhaust apparatus；
Described feeding machine 501 includes feeding motor, feeding reduction box, feed screw, feeding machine barrel and hopper, and feeding motor is merit
Rate 1.5 ~ 3KW；Feed screw Φ 45 ~ 60mm；Feeding cylinder bore Φ 45 ~ 60mm；Feed hopper volume L=100 ~ 200L, material
For rustless steel.
Main motor 2 502 uses alternating current generator or direct current generator, and rotating speed uses AC converter or DC speed regulator to adjust
Joint, motor output shaft is connected with twin screw reduction box 2 503 power shaft by shaft coupling, motor power (output) 90 ~ 200KW；
Reduction box 2 503: use parallel triple axle structure, gear ratio i=3 ~ 5, output speed 300 ~ 500RPM.
Described screw rod 2 504 is provided with screw arbor assembly；Described screw arbor assembly includes carrying spiral shell block, mixing spiral shell block, mediating spiral shell
Block, damping block and derotation spiral shell block, described screw rod is that screw arbor assembly arranged in series combines, and screw rod rotated versions is that twin screw is nibbled
Mould assembly rotating Vortex, screw slenderness ratio L/D=36:1 ~ 48:1, outer screw diameter Φ=61.5 ~ 94.5mm；Described machine barrel two is by 8 ~ 15
Joint cylinder is composed in series, machine barrel draw ratio L/D=36:1 ~ 48:1, and often joint cylinder is for including housing and liner, and housing uses 45# steel
For base material, built-in cyclic water channel is used for reducing barrel temperature, and outside parcel electric heater is for heating the material in machine barrel；Cylinder
Liner is that " ∞ " structure uses high-quality antifriction alloy thermally treated, machine barrel two internal diameter Φ=62 ~ 95mm.
Six, described sheet forming extrusion system includes double plunger type net-changing device 601, Melt Pump 602, sheet die
603；
Described net-changing device 601, is made up of Hydraulic Station and 2 plunger type net-changing devices, and Hydraulic Station leads to pressurization to be completed plunger screen changer
Move left and right, the design of double achieves does not shuts down draping function.Each net-changing device is provided with 1 oval shunting
Plate, flow distribution plate is fixed the impurity in metal screen melt filtration.
Melt Pump 602, pump housing material chrome-nickel steel, Nickel-Based Steel, heating element heater is rustless steel heating rod, discharge capacity 50
~ 100cm3/min, rotating speed 10 ~ 120rpm, driving motor power 5.5 ~ 7.5kw.
Being provided with runner in described sheet die 603, flow passage ends is discharging opening, and the die lip of discharging opening is provided with regulation bolt
And baffle plate, for regulating thickness and the width of lamellar melt, die lip width L=1000 ~ 1200mm, goods Breadth Maximum L=800 ~
1000mm, products thickness is δ=0.8～1.8mm.
Seven, described sheet forming auxiliary system includes calender 701, traction cooling bracket 702, edge-cutting device 703 and double
Station winder 704；
Calender 701: use three rollers or five rolling calender, by roller, actuating device, drum clearance adjustment device, water circulation warm
Control device, roller gap adjusting apparatus composition.Roller diameter is Φ 300 ~ 600mm, and width is L=1000 ~ 1300mm；Transmission fills
Putting stand alone type reduced ac motor 3 ~ 5.5KW, drum clearance adjustment device uses fluid pressure type regulation, range of accommodation 0～50mm；Water
Circulation attemperating unit is controlled by the water die heater of 3 or 5 platform independent, and quantity is corresponding with roller quantity, and accuracy of temperature control≤± 1 DEG C.
Traction cooling bracket 702: be made up of cooling bracket and traction machine.Cooling carrying roller length L=800 ~ 1200mm, external diameter
Ф=200~220mm.Traction machine motor is reducing motor, power 2.2 ~ 4KW；
Edge-cutting device 703: be made up of cut-off knife and scrap edge winding device, two, both sides cut-off knife can effectively excise waste material, make sheet material reach
To required width, cut the waste material got off and by scrap edge winding device rolling and reclaim；
Double-position winding machine 704: core is driven by torque motor, moment 10 ~ 15N.m.
The calendering of lamellar melt cooling and shaping that sheet die is extruded by calender are finished sheet, then cold by traction
But sheet material is cooled down and carries by bracket；Sheet edge is cut to the wide cut of requirement and reclaims by edge-cutting device；Double is received
Volume machine is for by final finished sheet rolling.
The above is only the preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For Yuan, on the premise of without departing from the technology of the present invention principle, it is also possible to make some improvement and deformation, these improve and deformation
Also should be regarded as protection scope of the present invention.
Claims (8)
1. a polymer is combined paper producing apparatus, it is characterised in that: include raw material feed system, mixing feed system, double spiral shell
Bar mixing granulator system, finished particle packaging system, twin-screw mixer extrusion system, sheet forming extrusion system and sheet forming
Auxiliary system；
Raw material feed system be used for the storage of raw material, conveying, quantitative weighing, then in individual ratio by feedstock transportation to mixing feeding
System；Mixing feed system is used for the bulk melt heated by each raw material, mixing is the most homogeneous, and feeds double spiral shell by drawing-in device
Bar mixing granulator system；Twin-screw mixer granulating system is for dissipating further for polymer melt compounding ingredients fully, being distributed all
Even melt, is made as solid particle of uniform size by pelletize and cooling device by melt；Finished particle packaging system is used
In solid particle being stored and packing, in case twin-screw mixer extrusion system uses；Twin-screw mixer extrusion system is by solid
Grain is melted and the degree of depth is mixing, mixing after melt enter sheet forming extrusion system；Polymer is melted by sheet forming extrusion system
Extrude to sheet forming auxiliary system from mould after body filtration, metering；Polymer melt is shaped also by sheet forming auxiliary system
It is cooled to polymer extrusion coating paper in uniform thickness, cuts rear rolling.
Polymer the most according to claim 1 is combined paper producing apparatus, it is characterised in that: described raw material feed system includes
Material negative pressure conveying device, fluid Supplying apparatus and automatic ration weighing device；Described material negative pressure conveying device and described liquid
Body feeding is all connected with described automatic ration weighing device；
Described material negative pressure conveying device includes that roots blower, material is defeated equipped with pulp-collecting box, the batch turning station of screw conveying device
Sending pipeline, operated pneumatic valve and Split filter device, described screw conveying device is driven by roots blower and is passed through by the raw material of pulp-collecting box
Material pipeline road flows to automatic ration weighing device, and described operated pneumatic valve arranges on Material pipeline road, powder body filter
The end on Material pipeline road, described powder body filter built-in cloth-bag type cartridge filter are set；
Described fluid Supplying apparatus includes liquid material head tank and liquid conveying oil pump；
Described automatic ration weighing device includes powder body gravimetric tank, liquid weighing tank and quantitative weighing sensing device, described powder body
Gravimetric tank top is provided with air filtration exhaust apparatus, and the top of described liquid weighing tank is provided with feeding mouth, and described feeding mouth passes through
Fluid pipeline is connected with fluid Supplying apparatus.
Polymer the most according to claim 1 is combined paper producing apparatus, it is characterised in that: described mixing feed system includes
High-speed mixer and taper forced feed machine；Described high-speed mixer includes pneumatic pot cover, the ladle body of sandwich, belt transmission
Mechanism and pneumatic type discharging device, described pot cover is provided with observation panel, charge door and air vent；It is provided with deflector in described ladle body
And stirrer paddle；Described taper forced feed machine include driving motor, reduction box, twin screw intermeshing screw, tapered cylinder and
Feed box, is configured with the heating rod the most admittedly heating conduction oil below described tapered cylinder and feed box.
Polymer the most according to claim 1 is combined paper producing apparatus, it is characterised in that: described twin-screw mixer pelletize system
System includes main motor one, parallel triple axle high torque reduction box one, screw rod one, machine barrel one and water ring pelletize subsidiary engine；
The output shaft of described main motor one is connected with the power shaft of reduction box one by shaft coupling, and described screw rod is provided with screw rod
Assembly；
Described screw rod one assembly includes carrying spiral shell block, mixing spiral shell block, mediating spiral shell block, damping block and derotation spiral shell block, described screw rod one
Combining for screw arbor assembly arranged in series, described machine barrel one is composed in series by 8 ~ 15 joint cylinders, and often joint cylinder is for including housing
And liner, the built-in cyclic water channel of described housing, outside is provided with electric heater；
Described water ring pelletize subsidiary engine include the fervent head of water ring die face, Water ring granulator, Water-circulating thermal cutting cover, water pump, water tank and from
Heart dewaterer forms；The described fervent head of water ring die face is made up of spreader and fervent die face, and Water ring granulator connection of getting home is cut
Grain blade, by spring level pressure blade on knife rest, patch floats in head die face, completes pelletizing action by rotation.
Polymer the most according to claim 1 is combined paper producing apparatus, it is characterised in that: described finished particle includes system
Including dry ebullated bed, homogenization silo and automatic packaging machine, material enters homogenizing after carrying out dried on dry ebullated bed
Feed bin, is then packed finished particle by automatic packaging machine.
Polymer the most according to claim 1 is combined paper producing apparatus, it is characterised in that: described twin-screw mixer extrusion is
System includes feeding machine, main motor two, reduction box two, screw rod two, machine barrel two and exhaust apparatus；Described feeding machine includes feeding electricity
Machine, feeding reduction box, feed screw, feeding machine barrel and hopper；The output shaft of described main motor two passes through shaft coupling and deceleration
The power shaft of case is connected, and described screw rod two is provided with screw arbor assembly；Described screw arbor assembly includes carrying spiral shell block, mixing spiral shell block, pinching
Closing spiral shell block, damping block and derotation spiral shell block, described screw rod two combines for screw arbor assembly arranged in series, and described machine barrel two is by 8 ~ 15
Joint cylinder is composed in series, and often joint cylinder is for including housing and liner, and the built-in cyclic water channel of described housing, outside is provided with electrical heating
Device.
Polymer the most according to claim 1 is combined paper producing apparatus, it is characterised in that: described sheet forming extrusion system
Including double plunger type net-changing device, Melt Pump, sheet die；Described net-changing device is provided with oval flow distribution plate, described shunting
Plate is provided with metal screen；Being provided with runner in described sheet die, flow passage ends is discharging opening, and the die lip of discharging opening is provided with tune
Joint bolt and baffle plate, for regulating thickness and the width of lamellar melt.
Polymer the most according to claim 1 is combined paper producing apparatus, it is characterised in that: described sheet forming auxiliary system
Including calender, traction cooling bracket, edge-cutting device and double-position winding machine, the lamellar melt that sheet die is extruded by calender
Calendering cooling and shaping are finished sheet, are then cooled down sheet material by traction cooling bracket and are carried；Edge-cutting device will
Sheet edge is cut to the wide cut of requirement and reclaims；Double-position winding machine is for by final finished sheet rolling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610747393.1A CN106182836B (en) | 2016-08-29 | 2016-08-29 | Polymer composite paper production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610747393.1A CN106182836B (en) | 2016-08-29 | 2016-08-29 | Polymer composite paper production equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106182836A true CN106182836A (en) | 2016-12-07 |
| CN106182836B CN106182836B (en) | 2019-04-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610747393.1A Active CN106182836B (en) | 2016-08-29 | 2016-08-29 | Polymer composite paper production equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106182836B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1134872A (en) * | 1995-08-31 | 1996-11-06 | 南亚塑胶工业股份有限公司 | Method for mfg. synthesized paper and products thereof |
| CN1245748A (en) * | 1999-07-28 | 2000-03-01 | 南亚塑胶工业股份有限公司 | Improved polypropylene pearlescent synthetic paper making method |
| CN105602215A (en) * | 2016-01-26 | 2016-05-25 | 深圳市绿自然生物降解科技有限公司 | Biodegradable heat-resistant sheet and preparation method thereof |
| CN206633459U (en) * | 2016-08-29 | 2017-11-14 | 江苏诚盟装备股份有限公司 | A kind of compound paper producing apparatus of polymer |
-
2016
- 2016-08-29 CN CN201610747393.1A patent/CN106182836B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1134872A (en) * | 1995-08-31 | 1996-11-06 | 南亚塑胶工业股份有限公司 | Method for mfg. synthesized paper and products thereof |
| CN1245748A (en) * | 1999-07-28 | 2000-03-01 | 南亚塑胶工业股份有限公司 | Improved polypropylene pearlescent synthetic paper making method |
| CN105602215A (en) * | 2016-01-26 | 2016-05-25 | 深圳市绿自然生物降解科技有限公司 | Biodegradable heat-resistant sheet and preparation method thereof |
| CN206633459U (en) * | 2016-08-29 | 2017-11-14 | 江苏诚盟装备股份有限公司 | A kind of compound paper producing apparatus of polymer |
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| Publication number | Publication date |
|---|---|
| CN106182836B (en) | 2019-04-09 |
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