CN106182836B - Polymer composite paper production equipment - Google Patents
Polymer composite paper production equipment Download PDFInfo
- Publication number
- CN106182836B CN106182836B CN201610747393.1A CN201610747393A CN106182836B CN 106182836 B CN106182836 B CN 106182836B CN 201610747393 A CN201610747393 A CN 201610747393A CN 106182836 B CN106182836 B CN 106182836B
- Authority
- CN
- China
- Prior art keywords
- screw
- sheet
- melt
- twin
- feed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- 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
-
- 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
-
- 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
Landscapes
- 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 equipments, and in particular, to a kind of compound paper producing apparatus of polymer.
Background technique
Traditional paper mainly has following disadvantage in process of production: raw material need timber and natural plant fibre, greatly
Amount destroys the forest reserves and causes environmental pollution.It is needed in entire production process with a large amount of water, while needing to add strong acid, strong
Alkali, bleaching powder and numerous organic chlorides, there are several important pollution sections such as boiling, washing, bleaching, generate " three wastes " and make
At pollution problem.Traditional paper complete set of equipments is at high price, occupied area is huge, needs early period that vast resources purchase is spent to set
Standby and construction workshop.
For the above-mentioned major defect of traditional paper, my company develops " a kind of polymer extrusion coating paper complete production unit ",
The complete set of equipments is for producing polymer extrusion coating paper.The extrusion coating paper is raw material without Fiber Materials such as timber, and production process is without " three
It is useless " discharge, while equipment cost is only 1/10th of traditional paper, and shared plant area very little.
Polymer extrusion coating paper is using synthetic resin such as polystyrene, polypropylene, polyethylene as primary raw material.It is produced according to final
Performance required by product, it is often the combination product of various polymer, inorganic powder and other organic matters.Extrusion coating paper " is made
The characteristics of paper " process, the actually process of synthetic resin casting film-forming, the tape casting is die head extruded velocity and casting roller
Linear velocity controls produced extrusion coating paper thickness there are biggish speed difference, by adjusting speed difference, can produce
The synthetic paper of various different-thickness.
Summary of the invention
It is raw to provide a kind of polymer extrusion coating paper in order to solve drawbacks described above and deficiency existing in the prior art by the present invention
Produce equipment.
In order to solve the above technical problems, the present invention provides a kind of compound paper producing apparatus of polymer, including raw material supply system
System, mixed feed system, twin-screw mixer granulating system, finished particle packaging system, twin-screw mixer extrusion system, sheet material at
Type extrusion system and sheet forming auxiliary system；
Raw material feed system is used for storage, the conveying, quantitative weighing of raw material, then extremely mixes feedstock transportation in ratio
Feed system；Mixed feed system is used for the heating of each raw material, mixes to uniform bulk melt, and is fed by drawing-in device
Twin-screw mixer granulating system；Twin-screw mixer granulating system be used for by the further compounding ingredients of polymer melt dissipate sufficiently, point
Melt is made as solid particle of uniform size by being granulated and cooling down equipment by the uniform melt of cloth；Finished particle packaging system
System is for storing and packing solid particle, in case twin-screw mixer extrusion system uses；Twin-screw mixer extrusion system will be consolidated
Simultaneously depth is kneaded body particle fusion, and the melt after mixing enters sheet forming extrusion system；Sheet forming extrusion system will polymerize
It is squeezed out from mold to sheet forming auxiliary system after object melt filtration, metering；Sheet forming auxiliary system determines polymer melt
Type is simultaneously cooled to polymer extrusion coating paper in homogeneous thickness, winds after cutting.
Further, the raw material feed system includes that material negative pressure conveying device, fluid Supplying apparatus and automatic ration claim
Refitting is set；The material negative pressure conveying device and the fluid Supplying apparatus are connected with the automatic ration weighing device；
The material negative pressure conveying device includes the batch turning station equipped with pulp-collecting box, screw conveying device, roots blower, object
Material conveying tube road, operated pneumatic valve and Split filter device, the screw conveying device are driven by roots blower by the raw material of pulp-collecting box
Automatic ration weighing device, the operated pneumatic valve setting material delivery pipe road, powder mistake are conveyed to by material delivery pipe road
The end on material delivery pipe road, cloth-bag type cartridge filter built in the powder filter is arranged in filter；
The fluid Supplying apparatus includes liquid material head tank and liquid conveying oil pump；
The automatic ration weighing device includes powder gravimetric tank, liquid weighing tank and quantitative weighing sensing device, described
Air filtration exhaust apparatus is equipped at the top of powder gravimetric tank, the top of the liquid weighing tank is equipped with feeding inlet, the feeding inlet
It is connected by fluid pipeline with fluid Supplying apparatus.
Further, the mixed feed system includes high-speed mixer and taper forced feed machine；The high-speed mixer
Including pneumatic pot cover, the ladle body of sandwich, belt gear and pneumatic type discharging device, the pot cover is equipped with observation
Mouth, feed opening and exhaust outlet；Deflector and stirrer paddle are equipped in the ladle body；The taper forced feed machine includes transmission electricity
Configured with forever below machine, reduction gearbox, twin-screw intermeshing screw, tapered cylinder and feed box, the tapered cylinder and feed box
Admittedly heating the heating rod of conduction oil.
Further, the twin-screw mixer granulating system include main motor one, parallel triple axle high torque reduction gearbox one,
Screw rod one, machine barrel one and water ring are granulated subsidiary engine；
The output shaft of the main motor one is connected by shaft coupling with the input shaft of reduction gearbox one, is set on the screw rod one
There is screw arbor assembly；
The screw arbor assembly includes transmission screw block, mixing screw block, kneading screw block, damping block and reverse screw block, the screw rod
One is composed for screw arbor assembly arranged in series, and the machine barrel one is composed in series by 8 ~ 15 section cylinders, every section cylinder be include shell
Body and liner, cyclic water channel built in the shell, outside are equipped with electric heater；
It includes the fervent head of water ring die face, Water ring granulator, Water-circulating thermal cutting cover, water pump, water tank that the water ring, which is granulated subsidiary engine,
It is formed with centrifugal dehydrator；The fervent head of water ring die face is made of spreader and fervent die face, and Water ring granulator is got home company
Pelletizing blade is connect, by spring level pressure blade on knife rest, patch is floated in head die face, completes pelletizing movement by rotation.
Further, it includes that dry ebullated bed, homogenization silo and automatic packaging machine, material exist that the finished particle, which includes system,
Enter homogenization silo after being dried on dry ebullated bed, then finished particle is packed by automatic packaging machine.
Further, the twin-screw mixer extrusion system includes feeder, main motor two, reduction gearbox two, screw rod two, machine
Cylinder two and exhaust apparatus；The feeder includes feeding motor, feeding reduction box, feed screw, feeding machine barrel and hopper；It is described
The output shaft of main motor two is connected by shaft coupling with the input shaft of reduction gearbox two, and the screw rod two is equipped with screw arbor assembly；
The screw arbor assembly includes transmission screw block, mixing screw block, kneading screw block, damping block and reverse screw block, and the screw rod two is screw rod
Component arranged in series is composed, and the machine barrel two is composed in series by 8 ~ 15 section cylinders, every section cylinder be include shell and liner,
Cyclic water channel built in the shell, outside are equipped with electric heater.
Further, the sheet forming extrusion system includes duplex station plunger type screen changer, Melt Pump, sheet die；Institute
It states net-changing device and is equipped with oval flow distribution plate, the flow distribution plate is equipped with metal screen；Runner, stream are equipped in the sheet die
Road end is discharge port, and the die lip of discharge port, which is equipped with, adjusts bolt and baffle, for adjusting the thickness and width of sheet-like melt.
Further, the sheet forming auxiliary system includes that calender, traction cooling bracket, edge-cutting device and double-station are received
Volume machine, the sheet-like melt calendering and cooling and shaping that calender squeezes out sheet die are finished sheet, then pass through traction cooling
Bracket is cooled down and is conveyed to sheet material；Sheet edge is cut to wide cut and the recycling of requirement by edge-cutting device；Double-station winding
Machine is used to wind final finished sheet.
Present invention advantageous effects achieved: a kind of compound paper producing apparatus of polymer provided by the invention, production
Three-waste free discharge in the process, while equipment cost is only 1/10th of traditional paper production equipment cost, shared plant area
It is smaller comprising raw material feed system, mixed feed system, twin-screw mixer granulating system, finished particle packaging system, double spiral shells
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 by a ratio by feedstock transportation to mixed feed system；Mixed feed system is for adding each raw material
Heat is mixed to uniform bulk melt, and feeds twin-screw mixer granulating system by drawing-in device；Twin-screw mixer is granulated system
It unites for the further compounding ingredients of polymer melt to be dissipated melt that is abundant, being evenly distributed, will be melted by being granulated and cooling down equipment
System is as solid particle of uniform size；Finished particle packaging system is for storing and packing solid particle, in case double spiral shells
Bar mixing extrusion system uses；Twin-screw mixer extrusion system is by solid particle melting and depth is kneaded, the melt after mixing into
Enter sheet forming extrusion system；Sheet forming extrusion system by polymer melt filter, metering after from mold squeeze out to sheet material at
Type auxiliary system；Polymer melt is formed and is cooled to polymer extrusion coating paper in homogeneous thickness by sheet forming auxiliary system, cuts out
It is wound after cutting.
Detailed description of the invention
Fig. 1-Fig. 3 schematic structural view of the invention.
Specific embodiment
The invention will be further described below in conjunction with the accompanying drawings.Following embodiment is only used for clearly illustrating the present invention
Technical solution, and not intended to limit the protection scope of the present invention.
As shown in Figure 1-3, the present invention provides a kind of compound paper producing apparatus of polymer, including raw material feed system, mixing
Feed system, twin-screw mixer granulating system, finished particle packaging system, twin-screw mixer extrusion system, sheet forming squeeze out
System and sheet forming auxiliary system；
Raw material feed system is used for storage, the conveying, quantitative weighing of raw material, then extremely mixes feedstock transportation in ratio
Feed system；Mixed feed system is used for the heating of each raw material, mixes to uniform bulk melt, and is fed by drawing-in device
Twin-screw mixer granulating system；Twin-screw mixer granulating system be used for by the further compounding ingredients of polymer melt dissipate sufficiently, point
Melt is made as solid particle of uniform size by being granulated and cooling down equipment by the uniform melt of cloth；Finished particle packaging system
System is for storing and packing solid particle, in case twin-screw mixer extrusion system uses；Twin-screw mixer extrusion system will be consolidated
Simultaneously depth is kneaded body particle fusion, and the melt after mixing enters sheet forming extrusion system；Sheet forming extrusion system will polymerize
It is squeezed out from mold to sheet forming auxiliary system after object melt filtration, metering；Sheet forming auxiliary system determines polymer melt
Type is simultaneously cooled to polymer extrusion coating paper in homogeneous thickness, winds after cutting.
One, the raw material feed system includes material negative pressure conveying device 101, fluid Supplying apparatus 102 and automatic ration
Weighing device 103；The material negative pressure conveying device 101 and the fluid Supplying apparatus 102 are weighed with the automatic ration
Device 103 is connected；
The material negative pressure conveying device 101 includes the batch turning station equipped with pulp-collecting box, screw conveying device, Luo Cifeng
Machine, material delivery pipe road, operated pneumatic valve and Split filter device, the screw conveying device are driven by roots blower by pulp-collecting box
Raw material is conveyed to automatic ration weighing device, the operated pneumatic valve setting material delivery pipe road, powder by material delivery pipe road
The end on material delivery pipe road, cloth-bag type cartridge filter built in the powder filter is arranged in body filter；Wherein, bolt conveying dress
Setting power of motor is 0.75-1.5KW, and roots blower power is 5.5-10.5KW, pipe diameter Ф=50 used in material delivery pipe road
~ 100mm, material are stainless steel
The fluid Supplying apparatus 102 includes that liquid material head tank and liquid convey oil pump；1 ~ 3m of raw material tank volume3, material
Stainless steel, thickness δ=1 ~ 3mm configure level detector and manually-operated gate, and liquid conveys 0.75 ~ 1.5kw of oil pump power, maximum stream flow
3700L/H；Liquid conducting pipes, material are stainless steel.
The automatic ration weighing device 103 includes powder gravimetric tank, liquid weighing tank and quantitative weighing sensing device, institute
It states and is equipped with air filtration exhaust apparatus at the top of powder gravimetric tank, the top of the liquid weighing tank is equipped with feeding inlet, the pan feeding
Mouth is connected by fluid pipeline with fluid Supplying apparatus；Powder weighing 1000 ~ 1500L of tank volume, material stainless steel, thickness δ=2 ~
4mm, liquid weighing 30 ~ 80L of tank volume, material stainless steel, thickness δ=2 ~ 4mm.
Two, the mixed feed system includes high-speed mixer 201 and taper forced feed machine 202；
The high-speed mixer 201 includes that pot cover described in pneumatic pot cover is equipped with observation panel, feed opening and exhaust outlet, material
304 weldments；The ladle body of sandwich, internal layer are 304 weldments, thickness 10mm, added with deflector and material inside ladle body
For the stirrer paddle of 304 casting, stirrer paddle quantity 2 ~ 4,800 ~ 1500L of interior ladle body total measurement (volume)；Belt gear, motor
150 ~ 250KW of power, revolving speed is by Frequency Converter Control；Pneumatic type discharging device, drain hole diameter 300mm；
The taper forced feed machine 202 includes driving motor, driving motor 7.5 ~ 11kw of power, frequency control；Slow down
Case, maximum output revolving speed 11rpm；Twin-screw intermeshing screw, counter rotating, 22 ° of taper, outside diameter φ 393mm, small end is straight
Diameter φ 70mm；Configured with the heating for heating conduction oil admittedly forever below tapered cylinder and feed box, the tapered cylinder and feed box
Stick；
Three, the twin-screw mixer granulating system includes main motor 1, parallel triple axle high torque reduction gearbox one
302, screw rod 303, machine barrel one and water ring are granulated subsidiary engine 304；
Main motor 1 uses alternating current generator or direct current generator, and revolving speed uses AC converter or DC speed regulator tune
Section, motor output shaft are connected by shaft coupling with one 302 input shaft of twin-screw reduction gearbox, 90 ~ 200KW of motor power (output)；
Parallel triple axle high torque reduction gearbox 1, transmission ratio i=3 ~ 5 export 300 ~ 500RPM of revolving speed；
The screw rod 1 is equipped with screw arbor assembly；The screw arbor assembly includes transmission screw block, mixing screw block, mediates spiral shell
Block, damping block and reverse screw block, the screw rod are that screw arbor assembly arranged in series is composed, and screw rod rotated versions are nibbled for twin-screw
Mould assembly rotating Vortex, screw slenderness ratio L/D=36:1 ~ 48:1, outer screw diameter Φ=61.5 ~ 94.5mm, the machine barrel one is by 8 ~ 15
Section cylinder is composed in series, and machine barrel draw ratio L/D=36:1 ~ 48:1, shell uses 45# steel for substrate, and built-in cyclic water channel is for dropping
Low barrel temperature, outside package electric heater are used to heat the material in machine barrel；Cylinder lining is " ∞ " structure using high-quality resistance to
Adjustment gold and thermally treated, cylinder bore Φ=62 ~ 95mm.
It includes the fervent head of water ring die face, Water ring granulator, Water-circulating thermal cutting cover, water pump, water that the water ring, which is granulated subsidiary engine 304,
Case and centrifugal dehydrator composition；The fervent head of water ring die face is made of spreader and fervent die face, and Water ring granulator is got home
Pelletizing blade is connected, by spring level pressure blade on knife rest, patch is floated in head die face, completes pelletizing movement by rotation.Water
The fervent cover material of ring is stainless steel, thickness δ=10 ~ 20mm；3 ~ 7.5KW of pump power, water tank material are stainless steel；Centrifugal dehydration
Machine shell and internal net-shaped drum material are stainless steel, and decelerating motor drives, pulley drive, and decelerating motor power 5.5 ~
11KW。
Four, the finished particle includes that system includes:
Dry ebullated bed 401,3000 ~ 4000L of cylinder volume；1000 ~ 2500kg of charge；Staving material: liner uses
The production of 2.0mm stainless steel, the production of shell 2mmA3 plate, centre plus special thermal insulation material；Dry heat power: 60KW, 15,4kw
∕ root；Heating method: electric heater for heating；Dehumidify cabinet 50*50*3mm；Power of fan: 5.5 ~ 7.5KW；Regenerate power of fan:
1.5~2.2KW；Regeneration heating power: heating rod 6, power 18KW；
Homogenization silo 402 is made of feed bin, pipeline and blower.8 ~ 10m3 of feed bin volume；3 ~ 5.5KW of power of fan, pipeline
Including pipeline, threeway and elbow, 130 ~ 160mm of diameter of phi；
Material enters homogenization silo after being dried on dry ebullated bed, then right by automatic packaging machine 403
Finished particle is packed.
Five, the twin-screw mixer extrusion system includes feeder 501, main motor 2 502, reduction gearbox 2 503, screw rod
2 504, machine barrel two and exhaust apparatus；
The feeder 501 includes feeding motor, feeding reduction box, feed screw, feeding machine barrel and hopper, feeding motor
For 1.5 ~ 3KW of power；45 ~ 60mm of feed screw Φ；45 ~ 60mm of feeding machine barrel internal diameter Φ；Feed hopper volume L=100 ~ 200L,
Material is stainless steel.
Main motor 2 502 uses alternating current generator or direct current generator, and revolving speed uses AC converter or DC speed regulator tune
Section, motor output shaft are connected by shaft coupling with 2 503 input shaft of twin-screw reduction gearbox, 90 ~ 200KW of motor power (output)；
Reduction gearbox 2 503: using parallel triaxial structure, and transmission ratio i=3 ~ 5 export 300 ~ 500RPM of revolving speed.
The screw rod 2 504 is equipped with screw arbor assembly；The screw arbor assembly includes transmission screw block, mixing screw block, mediates spiral shell
Block, damping block and reverse screw block, the screw rod are that screw arbor assembly arranged in series is composed, and screw rod rotated versions are nibbled for twin-screw
Mould assembly rotating Vortex, screw slenderness ratio L/D=36:1 ~ 48:1, outer screw diameter Φ=61.5 ~ 94.5mm；The machine barrel two is by 8 ~ 15
Section cylinder is composed in series, machine barrel draw ratio L/D=36:1 ~ 48:1, every section cylinder be include shell and liner, shell uses 45# steel
For substrate, built-in cyclic water channel is used to heat the material in machine barrel for reducing barrel temperature, outside package electric heater；Cylinder
Liner is that " ∞ " structure uses high-quality antifriction alloy and thermally treated, two internal diameter Φ=62 of machine barrel ~ 95mm.
Six, the sheet forming extrusion system includes duplex station plunger type screen changer 601, Melt Pump 602, sheet die
603；
The net-changing device 601 is made of hydraulic station and 2 plunger type screen changers, and the logical pressurization of hydraulic station is completed to change plunger
Wire stitcher moves left and right, and the design of double-station, which realizes, does not shut down draping function.Each net-changing device is equipped with 1 ellipse point
Flowing plate fixes the impurity in metal screen melt filtration on flow distribution plate.
Melt Pump 602, pump housing material chrome-nickel steel, Nickel-Based Steel, heating element are stainless steel heating rod, discharge capacity 50
~ 100cm3/min, 10 ~ 120rpm of revolving speed, 5.5 ~ 7.5kw of driving motor power.
Runner is equipped in the sheet die 603, flow passage ends are discharge port, and the die lip of discharge port, which is equipped with, adjusts bolt
And baffle, for adjusting the thickness and width of sheet-like melt, die lip width L=1000 ~ 1200mm, product maximum width L=800 ~
1000mm, products thickness are δ=0.8~1.8mm.
Seven, the sheet forming auxiliary system includes calender 701, traction cooling bracket 702, edge-cutting device 703 and double
Station winder 704；
Calender 701: three rollers or five rolling calender are used, is followed by roller, transmission device, drum clearance adjustment device, water
Ring temperature control device, roller gap adjustment device composition.Roller diameter is 300 ~ 600mm of Φ, and width is L=1000 ~ 1300mm；It passes
Dynamic device stand alone type 3 ~ 5.5KW of reduced ac motor, drum clearance adjustment device are adjusted using fluid pressure type, and adjustable range 0~
50mm；Water recycles temperature control device and is controlled by 3 or 5 independent water die heaters, and quantity is corresponding with roller quantity, and accuracy of temperature control≤±
1℃。
Draw cooling bracket 702: by cooling bracket and traction link seat at.Cooling carrying roller length L=800 ~ 1200mm, outer diameter
Ф=200~220mm.Dragger motor is decelerating motor, 2.2 ~ 4KW of power；
Edge-cutting device 703: being made of cut-off knife and scrap edge winding device, and the cut-off knife of two sides two can effectively cut off waste material, makes piece
Material reaches required width, cuts the waste material to get off and is wound and recycled by scrap edge winding device；
Double-position winding machine 704: core is driven by torque motor, 10 ~ 15N.m of torque.
The sheet-like melt calendering and cooling and shaping that calender squeezes out sheet die are finished sheet, then cold by drawing
But bracket is cooled down and is conveyed to sheet material；Sheet edge is cut to wide cut and the recycling of requirement by edge-cutting device；Double-station is received
Volume machine is used to wind final finished sheet.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For member, without departing from the technical principles of the invention, several improvement and deformations can also be made, these improvement and deformations
Also it should be regarded as protection scope of the present invention.
Claims (1)
1. a kind of compound paper producing apparatus of polymer, it is characterised in that: including raw material feed system, mixed feed system, double spiral shells
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 is used for storage, the conveying, quantitative weighing of raw material, then by a ratio by feedstock transportation to mixed feed
System；Mixed feed system is used for the heating of each raw material, mixes to uniform bulk melt, and feeds double spiral shells by drawing-in device
Bar mixing granulator system；Twin-screw mixer granulating system is used to the further compounding ingredients of polymer melt dissipating abundant, distribution
Melt is made as solid particle of uniform size by being granulated and cooling down equipment by even melt；Finished particle packaging system is used
In storing and packing solid particle, in case twin-screw mixer extrusion system uses；Twin-screw mixer extrusion system is by solid
Simultaneously depth is kneaded for grain melting, and the melt after mixing enters sheet forming extrusion system；Sheet forming extrusion system melts polymer
It is squeezed out from mold to sheet forming auxiliary system after body filtering, metering；Polymer melt is formed simultaneously by sheet forming auxiliary system
It is cooled to polymer extrusion coating paper in homogeneous thickness, is wound after cutting；
The mixed feed system includes high-speed mixer and taper forced feed machine；The high-speed mixer includes pneumatic pot
Lid, the ladle body of sandwich, belt gear and pneumatic type discharging device, the pot cover be equipped with observation panel, feed opening and
Exhaust outlet；Deflector and stirrer paddle are equipped in the ladle body；The taper forced feed machine include driving motor, reduction gearbox,
Configured with heating conduction oil below twin-screw intermeshing screw, tapered cylinder and feed box, the tapered cylinder and feed box
Heating rod；
The raw material feed system includes material negative pressure conveying device, fluid Supplying apparatus and automatic ration weighing device；It is described
Material negative pressure conveying device and the fluid Supplying apparatus are connected with the automatic ration weighing device；
The material negative pressure conveying device includes the batch turning station equipped with pulp-collecting box, screw conveying device, roots blower, and material is defeated
Pipeline, operated pneumatic valve and Split filter device are sent, the screw conveying device is driven by roots blower passes through the raw material of pulp-collecting box
Material delivery pipe road is conveyed to automatic ration weighing device, the operated pneumatic valve setting material delivery pipe road, powder filter
The end on material delivery pipe road, cloth-bag type cartridge filter built in the powder filter are set；
The fluid Supplying apparatus includes liquid material head tank and liquid conveying oil pump；
The automatic ration weighing device includes powder gravimetric tank, liquid weighing tank and quantitative weighing sensing device, the powder
Air filtration exhaust apparatus is equipped at the top of gravimetric tank, the top of the liquid weighing tank is equipped with feeding inlet, and the feeding inlet passes through
Fluid pipeline is connected with fluid Supplying apparatus；
The twin-screw mixer granulating system includes main motor one, parallel triple axle high torque reduction gearbox one, screw rod one, machine barrel
One and water ring be granulated subsidiary engine；
The output shaft of the main motor one is connected by shaft coupling with the input shaft of reduction gearbox one, and the screw rod is equipped with screw rod
Component；
One component of screw rod includes transmission screw block, mixing screw block, kneading screw block, damping block and reverse screw block, the screw rod one
Be composed for screw arbor assembly arranged in series, the machine barrel one is composed in series by 8~15 section cylinders, every section cylinder be include shell
And liner, cyclic water channel built in the shell, outside are equipped with electric heater；
The water ring be granulated 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 composition；The fervent head of water ring die face is made 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 is floated in head die face, completes pelletizing movement by rotation；
The finished particle packaging system includes dry ebullated bed, homogenization silo and automatic packaging machine, and material is in dry ebullated bed
On be dried after enter homogenization silo, then finished particle is packed by automatic packaging machine；
The twin-screw mixer extrusion system includes feeder, main motor two, reduction gearbox two, screw rod two, machine barrel two and exhaust
Device；The feeder includes feeding motor, feeding reduction box, feed screw, feeding machine barrel and hopper；The main motor two
Output shaft be connected with the input shaft of reduction gearbox by shaft coupling, the screw rod two is equipped with screw arbor assembly；The screw arbor assembly
Including transmission screw block, mixing screw block, kneading screw block, damping block and reverse screw block, the screw rod two is screw arbor assembly arranged in series
Be composed, the machine barrel two is composed in series by 8~15 section cylinders, every section cylinder be include shell and liner, in the shell
Cyclic water channel is set, outside is equipped with electric heater；
The sheet forming extrusion system includes duplex station plunger type screen changer, Melt Pump, sheet die；It is set on the net-changing device
There is oval flow distribution plate, the flow distribution plate is equipped with metal screen；Runner is equipped in the sheet die, flow passage ends are discharging
Mouthful, the die lip of discharge port, which is equipped with, adjusts bolt and baffle, for adjusting the thickness and width of sheet-like melt；
The sheet forming auxiliary system includes calender, traction cooling bracket, edge-cutting device and double-position winding machine, calender
By sheet die squeeze out sheet-like melt calendering and cooling and shaping be finished sheet, then by traction cooling bracket to sheet material into
Row is cooling and conveys；Sheet edge is cut to wide cut and the recycling of requirement by edge-cutting device；Double-position winding machine is used for will be final
Finished sheet winding.
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 CN106182836A (en) | 2016-12-07 |
| CN106182836B true CN106182836B (en) | 2019-04-09 |
Family
ID=57526490
Family Applications (1)
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106182836A (en) | 2016-12-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102729446A (en) | Linkage production method and device for rubber hose extrusion | |
| CN201253940Y (en) | Double driving type planet screw rod tape casting extruder | |
| NO302105B1 (en) | Process for preparing a composite product | |
| CN205291525U (en) | Plastic extrusion forming machine | |
| CN102107468B (en) | Large-sized mixing and extrusion granulating set | |
| CN102785301B (en) | Waste plastics treating and utilizing system | |
| CN101585227B (en) | Planetary screw drooling extruder | |
| CN108859190A (en) | A kind of new material stone paper production production line | |
| CN212949081U (en) | Double-screw extruder for polyacrylic resin | |
| CN206633459U (en) | A kind of compound paper producing apparatus of polymer | |
| CN104354301A (en) | Degradable sheet double-stage extrusion calendaring complete equipment | |
| CN204222201U (en) | Degraded sheet material two rank extrusion calendaring is molded into complete equipment | |
| WO2021051644A1 (en) | Crawler-type mixing apparatus for long fiber reinforced thermoplastic composite material | |
| CN202656344U (en) | Waste plastic disposal and utilization system | |
| CN104816401B (en) | The Granulation Equipments of paraffin and method | |
| CN110154359A (en) | A method of reclaimed rubber is refined and refined using Co rotating Twin Screw Extrusion | |
| CN106182836B (en) | Polymer composite paper production equipment | |
| CN203410011U (en) | Planetary screw casting extruder | |
| CN201253939Y (en) | Single driving type planet screw rod tape casting extruder | |
| CN106832396A (en) | Full-automatic plasticizing desulfurizing machine | |
| CN205704816U (en) | A kind of powdery paints extrusion device | |
| CN104369345A (en) | Planetary screw casting extruder | |
| CN204687304U (en) | A kind of anticlogging high benefit screw extruder | |
| CN208452354U (en) | A kind of new material stone paper production production line | |
| CN206048580U (en) | A kind of foamed materialss reclaim comminutor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201217 Address after: No.22, Liuzhou North Road, Taishan street, Jiangbei new district, Nanjing, Jiangsu Province, 210000 Patentee after: NANJING CHENGMENG EXTRUSION EQUIPMENT Co.,Ltd. Address before: No.22, Liuzhou North Road, Taishan Park, high tech Zone, Nanjing, Jiangsu Province, 210031 Patentee before: JIANGSU CENMEN EQUIPMENT Corp.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220524 Address after: 210000 No. 10 Julong Road, Jiangbei new district, Nanjing, Jiangsu Patentee after: JIANGSU CENMEN EQUIPMENT Corp.,Ltd. Address before: No.22, Liuzhou North Road, Taishan street, Jiangbei new district, Nanjing, Jiangsu Province, 210000 Patentee before: NANJING CHENGMENG EXTRUSION EQUIPMENT CO.,LTD. |
|
| TR01 | Transfer of patent right |