CN206633459U - A kind of compound paper producing apparatus of polymer - Google Patents

A kind of compound paper producing apparatus of polymer Download PDF

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Publication number
CN206633459U
CN206633459U CN201621006195.1U CN201621006195U CN206633459U CN 206633459 U CN206633459 U CN 206633459U CN 201621006195 U CN201621006195 U CN 201621006195U CN 206633459 U CN206633459 U CN 206633459U
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CN
China
Prior art keywords
screw
sheet
twin
melt
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.)
Withdrawn - After Issue
Application number
CN201621006195.1U
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Chinese (zh)
Inventor
马宏
张宏革
房宾
马宇嘉
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JIANGSU CENMEN EQUIPMENT CORP Ltd
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JIANGSU CENMEN EQUIPMENT CORP Ltd
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Priority to CN201621006195.1U priority Critical patent/CN206633459U/en
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Publication of CN206633459U publication Critical patent/CN206633459U/en
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58—Component parts, details or accessories; Auxiliary operations
    • B29B7/60—Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material
    • 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
    • B29C43/22—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of indefinite length
    • B29C43/24—Calendering
    • 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
    • B29C43/32—Component parts, details or accessories; Auxiliary operations
    • B29C43/34—Feeding the material to the mould or the compression means
    • 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
    • B29C43/32—Component parts, details or accessories; Auxiliary operations
    • B29C43/52—Heating or cooling
    • 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
    • B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07—Flat, e.g. panels
    • B29C48/08—Flat, e.g. panels flexible, e.g. films
    • 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
    • B29C48/30—Extrusion nozzles or dies
    • B29C48/305—Extrusion nozzles or dies having a wide opening, e.g. for forming sheets
    • 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
    • B29C48/365—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using pumps, e.g. piston pumps
    • 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
    • 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
    • B29C48/50—Details of extruders
    • B29C48/69—Filters or screens for the moulding material
    • B29C48/691—Arrangements for replacing filters, e.g. with two parallel filters for alternate use
    • 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
    • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911—Cooling
    • B29C48/9135—Cooling of flat articles, e.g. using specially adapted supporting means
    • B29C48/914—Cooling of flat articles, e.g. using specially adapted supporting means cooling drums
    • 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
    • B29B7/00—Mixing; Kneading
    • B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/48—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
    • 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
    • B29B7/00—Mixing; Kneading
    • B29B7/80—Component parts, details or accessories; Auxiliary operations
    • B29B7/82—Heating or cooling
    • 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
    • B29C43/32—Component parts, details or accessories; Auxiliary operations
    • B29C43/34—Feeding the material to the mould or the compression means
    • B29C2043/3433—Feeding the material to the mould or the compression means using dispensing heads, e.g. extruders, placed over or apart from the moulds

Abstract

The utility model 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 extrusion system and sheet forming auxiliary system；Equipment three-waste free discharge, while equipment cost is only 1/10th of traditional paper production equipment cost in process of production, shared plant area is smaller.

Description

A kind of compound paper producing apparatus of polymer
Technical field
A kind of production equipment is the utility model is related to, in particular it relates to a kind of compound paper producing apparatus of polymer.
Background technology
Traditional paper mainly possesses following shortcoming in process of production：Raw material need timber and natural plant fibre, greatly Amount destroys the forest reserves and causes environmental pollution.Needed in whole production process with substantial amounts of water, while need to add strong acid, strong Alkali, bleaching powder and numerous organic chlorides, several important pollution sections such as boiling, washing, bleaching be present, produce " three wastes " and make Into pollution problem.Traditional paper complete set of equipments price is high, floor space is huge, needs early stage to spend ample resources purchase to set Standby and construction factory building.
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 used to produce 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.According to final production 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 process of paper " process, actually synthetic resin casting film-forming, it is the rotation of die head extruded velocity and casting roller the characteristics of the tape casting Turn linear velocity and larger speed difference be present, produced extrusion coating paper thickness is controlled by regulating the speed difference, can produce each The synthetic paper of kind different-thickness.
Utility model content
The utility model is in order to solve drawbacks described above present in prior art and deficiency, there is provided a kind of polymer is compound Paper producing apparatus.
In order to solve the above technical problems, the utility model provides a kind of compound paper producing apparatus of polymer, including raw material supplies To system, mixing feed system, twin-screw mixer granulating system, finished particle packaging system, twin-screw mixer extrusion system, piece Material is molded extrusion system and sheet forming auxiliary system；
Raw material feed system is used for the storage, conveying, quantitative weighing of raw material, then extremely mixes feedstock transportation in a ratio Feed system；Mixing feed system is used for the heating of each raw material, mixed to homogeneous 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 fully, point The uniform melt of cloth, melt is made as solid particle of uniform size with cooling device by being granulated；Finished particle packaging system Unite for storing and packing solid particle, in case twin-screw mixer extrusion system uses；Twin-screw mixer extrusion system will be solid Simultaneously depth is kneaded body particle fusion, and the melt after mixing enters sheet forming extrusion system；Sheet forming extrusion system will polymerize Extruded after thing melt filtration, metering from mould to sheet forming auxiliary system；Sheet forming auxiliary system determines polymer melt Type is simultaneously cooled to polymer extrusion coating paper in uniform thickness, is wound after cutting.
Further, the raw material feed system claims including material negative pressure conveying device, fluid Supplying apparatus and automatic ration Refitting is put；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, thing Material conveying tube road, operated pneumatic valve and Split filter device, the screw conveying device are driven the raw material of pulp-collecting box by roots blower Automatic ration weighing device is conveyed to by material delivery pipe road, the operated pneumatic valve is set on material delivery pipe road, powder mistake Filter sets the end on material delivery pipe road, cloth-bag type cartridge filter built in the powder 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 provided with the top of powder gravimetric tank, the top of the liquid weighing tank is provided with feeding mouth, the feeding mouth It is connected by fluid pipeline with fluid Supplying apparatus.
Further, the mixing 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 provided with observation Mouth, charge door and exhaust outlet；Deflector and stirrer paddle are provided with the ladle body；The taper forced feed machine includes transmission electricity Machine, reduction box, twin-screw intermeshing screw, tapered cylinder and feed box, tapered cylinder and the feed box lower section are configured with forever Admittedly heat 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 box 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 that screw arbor assembly arranged in series combines, and the machine barrel one is composed in series by 8~15 section cylinders, and it is to include often to save cylinder Housing and liner, cyclic water channel built in the housing, outside are provided with electric heater；
The water ring, which is granulated subsidiary engine, includes the fervent head of water ring die face, Water ring granulator, Water-circulating thermal cutting cover, water pump, water tank Formed with centrifugal dehydrator；The fervent head of water ring die face is made up of spreader and fervent die face, and Water ring granulator is got home company Pelletizing blade is connect, is floated on knife rest by spring level pressure blade, patch in head die face, pelletizing action is completed by rotating.
Further, the finished particle exists including system including drying ebullated bed, homogenization silo and automatic packaging machine, material Dry and enter homogenization silo after carrying out drying process on ebullated bed, then finished particle is packed by automatic packaging machine.
Further, the twin-screw mixer extrusion system includes feeding machine, main motor two, reduction box two, screw rod two, machine Cylinder two and exhaust apparatus；The feeding machine 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 box two, and the screw rod two is provided 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 combined, and the machine barrel two is composed in series by 8~15 section cylinders, and it is to include housing and interior often to save cylinder Lining, cyclic water channel built in the housing, outside is provided with electric heater.
Further, the sheet forming extrusion system includes duplex station plunger type screen changer, Melt Pump, sheet die；Institute State net-changing device and be provided with oval flow distribution plate, the flow distribution plate is provided with metal screen；Runner is provided with the sheet die, is flowed Road end is discharging opening, and the die lip of discharging opening is provided with regulating bolt and baffle plate, for adjusting the thickness and width of sheet-like melt.
Further, the sheet forming auxiliary system includes calender, traction cooling bracket, edge-cutting device and double receipts Volume machine, calender rolls the sheet-like melt that sheet die is extruded and cooling and shaping is finished sheet, then passes through and draws cooling Bracket is cooled down and conveyed to sheet material；Sheet edge is cut to wide cut and the recovery of requirement by edge-cutting device；Double is wound Machine is used to wind final finished sheet.
The advantageous effects that the utility model is reached：A kind of polymer extrusion coating paper production provided by the utility model is set It is standby, three-waste free discharge in production process, while equipment cost is only 1/10th of traditional paper production equipment cost, shared factory Room area is smaller, and it includes raw material feed system, mixing feed system, twin-screw mixer granulating system, finished particle packaging system System, twin-screw mixer extrusion system, sheet forming extrusion system and sheet forming auxiliary system；Raw material feed system is used for raw material Storage, conveying, quantitative weighing, then in individual ratio by feedstock transportation to mixing feed system；Mixing feed system is used for will Each raw material heating, mix to homogeneous bulk melt, and twin-screw mixer granulating system is fed by drawing-in device；Double-screw mixing Refining granulating system is used to the further compounding ingredients of polymer melt dissipating melt that is abundant, being evenly distributed, by being granulated and cooling down Melt is made as solid particle of uniform size by equipment；Finished particle packaging system is used to solid particle is stored and packed, In case twin-screw mixer extrusion system uses；Solid particle melting and depth are kneaded by twin-screw mixer extrusion system, after mixing Melt enter sheet forming extrusion system；Sheet forming extrusion system filters polymer melt, measure after extruded from mould To sheet forming auxiliary system；Polymer melt is shaped and is cooled to polymer in uniform thickness and answered by sheet forming auxiliary system Combined paper, wound after cutting.
Brief description of the drawings
The raw material feed system, mixing feed system and twin-screw mixer granulating system structural representation of Fig. 1 the utility model Figure；
The finished particle packaging system structural representation of Fig. 2 the utility model；
The twin-screw mixer extrusion system, sheet forming extrusion system and sheet forming auxiliary system of Fig. 3 the utility model Structural representation；
Embodiment
The utility model is further described below in conjunction with the accompanying drawings.Following examples are only used for clearly illustrating this The technical scheme of utility model, and the scope of protection of the utility model can not be limited with this.
As Figure 1-3, a kind of compound paper producing apparatus of polymer of the utility model offer, including raw material feed system, Mix feed system, twin-screw mixer granulating 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 the storage, conveying, quantitative weighing of raw material, then extremely mixes feedstock transportation in a ratio Feed system；Mixing feed system is used for the heating of each raw material, mixed to homogeneous 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 fully, point The uniform melt of cloth, melt is made as solid particle of uniform size with cooling device by being granulated；Finished particle packaging system Unite for storing and packing solid particle, in case twin-screw mixer extrusion system uses；Twin-screw mixer extrusion system will be solid Simultaneously depth is kneaded body particle fusion, and the melt after mixing enters sheet forming extrusion system；Sheet forming extrusion system will polymerize Extruded after thing melt filtration, metering from mould to sheet forming auxiliary system；Sheet forming auxiliary system determines polymer melt Type is simultaneously cooled to polymer extrusion coating paper in uniform thickness, is wound 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 pulp-collecting box by roots blower Raw material is conveyed to automatic ration weighing device by material delivery pipe road, and the operated pneumatic valve is set on material delivery pipe road, powder Body filter sets the end on material delivery pipe road, cloth-bag type cartridge filter built in the powder filter；Wherein, bolt conveying dress It is 0.75-1.5KW to put power of motor, and roots blower power is 5.5-10.5KW, pipe diameter Ф used in material delivery pipe road= 50~100mm, material are stainless steel
The fluid Supplying apparatus 102 includes liquid material head tank and liquid conveying oil pump；1~3m of raw material tank volume3, material Stainless steel, thickness δ=1~3mm, configure level detector and manually-operated gate, liquid conveying oil pump 0.75~1.5kw of power, max-flow Measure 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 State and be provided with air filtration exhaust apparatus at the top of powder gravimetric tank, the top of the liquid weighing tank is provided with feeding mouth, the pan feeding Mouth is connected by fluid pipeline with fluid Supplying apparatus；Powder is weighed 1000~1500L of tank volume, material stainless steel, and thickness δ= 2~4mm, liquid weighing 30~80L of tank volume, material stainless steel, thickness δ=2~4mm.
Two, the mixing feed system includes high-speed mixer 201 and taper forced feed machine 202；
The high-speed mixer 201 is provided with observation panel, charge door and exhaust outlet, material including pot cover described in pneumatic pot cover 304 weldments；The ladle body of sandwich, its 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, electricity 150~250KW of acc power, rotating 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 rotating speed 11rpm；Twin-screw intermeshing screw, counter rotating, 22 ° of taper, outside diameter393mm, small end are straight Footpath70mm；Tapered cylinder and feed box, tapered cylinder and the feed box lower section are configured with the heating for heating conduction oil admittedly forever Rod；
Three, the twin-screw mixer granulating system includes main motor 1, parallel triple axle high torque reduction gearbox one 302nd, 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 rotating speed is adjusted using AC converter or DC speed regulator Section, motor output shaft are connected by shaft coupling with the input shaft of twin-screw reduction box 1, and motor power (output) 90~ 200KW；
Parallel triple axle high torque reduction gearbox 1, gearratio i=3~5,300~500RPM of output speed；
The screw rod 1 is provided 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 combines, 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 by 8~15 section cylinders are composed in series, machine barrel draw ratio L/D=36:1~48:1, housing uses 45# steel as base material, built-in recirculated water Road is used to reduce barrel temperature, and outside parcel electric heater is used to heat the material in machine barrel；Cylinder lining is that " ∞ " structure is adopted With high-quality antifriction alloy and thermally treated, cylinder bore Φ=62~95mm.
The water ring, which is granulated 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 fervent head of water ring die face is made up of spreader and fervent die face, and Water ring granulator is got home Pelletizing blade is connected, is floated on knife rest by spring level pressure blade, patch in head die face, pelletizing action is completed by rotating.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；Centrifugation is de- Water dispenser shell and internal net-shaped drum material are stainless steel, and reducing motor drives, pulley drive, reducing motor power 5.5 ~11KW.
Four, the finished particle includes including system：
Dry ebullated bed 401,3000~4000L of cylinder volume；1000~2500kg of charge；Staving material：Inner bag is adopted Made of 2.0mm stainless steels, shell 2mmA3 plates make, centre plus special insulation material；Dry heat power：60KW, 15, 4kw/ roots；Mode of heating：Electric heater for heating；Dehumidify casing 50*50*3mm；Power of fan：5.5~7.5KW；Regenerate blower fan work( Rate：1.5~2.2KW；Regenerate heating power：Heating rod 6, power 18KW；
Homogenization silo 402, it is made up of feed bin, pipeline and blower fan.8~10m of feed bin volume3；3~5.5KW of power of fan, pipe Road includes pipeline, threeway and elbow, 130~160mm of diameter of phi；
Material enters homogenization silo after carrying out drying process on ebullated bed is dried, then right by automatic packaging machine 403 Finished particle is packed.
Five, the 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；
The feeding machine 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 are stainless steel.
Main motor 2 502 uses alternating current generator or direct current generator, and rotating speed is adjusted using AC converter or DC speed regulator Section, motor output shaft are connected by shaft coupling with the input shaft of twin-screw reduction box 2 503, and motor power (output) 90~ 200KW；
Reduction box 2 503：Using parallel triaxial structure, gearratio i=3~5,300~500RPM of output speed.
The screw rod 2 504 is provided 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 combines, 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 by 8~15 section cylinders are composed in series, machine barrel draw ratio L/D=36:1~48:1, it is to include housing and liner often to save cylinder, and housing is adopted It is base material with 45# steel, built-in cyclic water channel is used to reduce barrel temperature, and outside parcel electric heater is used to heat the thing in machine barrel Material；Cylinder lining is that " ∞ " structure uses high-quality antifriction alloy and thermally treated, internal diameter Φ=62 of machine barrel two~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, it is made up of hydraulic station and 2 plunger type screen changers, the logical pressurization of hydraulic station is completed to change plunger Wire stitcher moves left and right, and the design of double, which realizes, does not shut down draping function.Each net-changing device is provided with 1 ellipse point Flowing plate, the impurity in metal screen melt filtration is fixed on flow distribution plate.
Melt Pump 602, pump housing material chrome-nickel steel, Nickel-Based Steel, heating element heater are stainless steel heating rod, discharge capacity 50 ~100cm3/min, 10~120rpm of rotating speed, 5.5~7.5kw of driving motor power.
Runner is provided with the sheet die 603, flow passage ends are discharging opening, and the die lip of discharging opening is provided with regulating bolt And baffle plate, for adjusting the thickness and width of sheet-like melt, die lip width L=1000~1200mm, product Breadth Maximum 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：Using three rollers or five rolling calender, followed by roller, transmission device, drum clearance adjustment device, water Ring temperature control device, roller gap adjusting apparatus composition.Roller diameter is 300~600mm of Φ, and width is L=1000~1300mm； Transmission 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 circulation temperature control device 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 into.Carrying roller length L=800~1200mm is cooled down, outside Footpath Ф=200~220mm.Hauling machine motor is reducing motor, 2.2~4KW of power；
Edge-cutting device 703：It is made up of cut-off knife and scrap edge winding device, the cut-off knife of both sides two can effectively cut off waste material, make piece Material reaches required width, cuts the waste material to get off and is wound and reclaimed by scrap edge winding device；
Double-position winding machine 704：Core is driven by torque motor, 10~15N.m of torque.
Calender rolls the sheet-like melt that sheet die is extruded and cooling and shaping is finished sheet, then cold by drawing But bracket is cooled down and conveyed to sheet material；Sheet edge is cut to wide cut and the recovery of requirement by edge-cutting device；Double is received Volume machine is used to wind final finished sheet.
Described above is only preferred embodiment of the present utility model, it is noted that for the common skill of the art For art personnel, on the premise of the utility model technical principle is not departed from, some improvement and deformation can also be made, these change Enter and deform and also should be regarded as the scope of protection of the utility model.

Claims (1)

  1. A kind of 1. compound paper producing apparatus of polymer, it is characterised in that：Including raw material feed system, mixing 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 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 heating of each raw material, mixed to homogeneous 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 Even melt, melt is made as solid particle of uniform size with cooling device by being granulated；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 Extruded after body filtering, metering from mould to sheet forming auxiliary system；Sheet forming auxiliary system shapes polymer melt simultaneously Polymer extrusion coating paper in uniform thickness is cooled to, is wound after cutting；
    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, and roots blower, 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, and the operated pneumatic valve is set on 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 provided with the top of gravimetric tank, the top of the liquid weighing tank is provided with feeding mouth, and the feeding mouth passes through Fluid pipeline is connected with fluid Supplying apparatus；
    The mixing 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 provided with observation panel, charge door and Exhaust outlet；Deflector and stirrer paddle are provided with the ladle body；The taper forced feed machine include driving motor, reduction box, Twin-screw intermeshing screw, tapered cylinder and feed box, tapered cylinder and the feed box lower section is configured with heats heat conduction admittedly forever The heating rod of oil；
    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 box one, and the screw rod is provided with screw rod Component；
    The component of screw rod one includes transmission screw block, mixing screw block, kneading screw block, damping block and reverse screw block, the screw rod one Combined for screw arbor assembly arranged in series, the machine barrel one is composed in series by 8~15 section cylinders, and it is to include housing often to save cylinder And liner, cyclic water channel built in the housing, outside are provided 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 forms；The 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, floated on knife rest by spring level pressure blade, patch in head die face, pelletizing action is completed by rotating；
    The finished particle, which includes system, to be included drying ebullated bed, homogenization silo and automatic packaging machine, and material is drying ebullated bed Enter homogenization silo after upper carry out drying process, then finished particle is packed by automatic packaging machine；
    The twin-screw mixer extrusion system includes feeding machine, main motor two, reduction box two, screw rod two, machine barrel two and exhaust Device；The feeding machine includes feeding motor, feeding reduction box, feed screw, feeding machine barrel and hopper；The main motor two Output shaft be connected by shaft coupling with the input shaft of reduction box, the screw rod two is provided 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 Combine, the machine barrel two is composed in series by 8~15 section cylinders, and it is to include housing and liner often to save cylinder, in the housing Cyclic water channel is put, outside is provided with electric heater；
    The sheet forming extrusion system includes duplex station plunger type screen changer, Melt Pump, sheet die；Set on the net-changing device There is oval flow distribution plate, the flow distribution plate is provided with metal screen；Runner is provided with the sheet die, flow passage ends are discharging Mouthful, the die lip of discharging opening is provided with regulating bolt and baffle plate, 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 Sheet-like melt calendering and cooling and shaping by sheet die extrusion are finished sheet, and then sheet material is entered by drawing cooling bracket Row is cooled down and conveyed；Sheet edge is cut to wide cut and the recovery of requirement by edge-cutting device；Double-position winding machine is used for will be final Finished sheet winding.
CN201621006195.1U 2016-08-29 2016-08-29 A kind of compound paper producing apparatus of polymer Withdrawn - After Issue CN206633459U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621006195.1U CN206633459U (en) 2016-08-29 2016-08-29 A kind of compound paper producing apparatus of polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621006195.1U CN206633459U (en) 2016-08-29 2016-08-29 A kind of compound paper producing apparatus of polymer

Publications (1)

Publication Number Publication Date
CN206633459U true CN206633459U (en) 2017-11-14

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106182836A (en) * 2016-08-29 2016-12-07 江苏诚盟装备股份有限公司 Polymer composite paper production equipment
CN115384075A (en) * 2022-08-29 2022-11-25 中化工程沧州冷却技术有限公司 Production process of filler for cooling tower

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106182836A (en) * 2016-08-29 2016-12-07 江苏诚盟装备股份有限公司 Polymer composite paper production equipment
CN106182836B (en) * 2016-08-29 2019-04-09 江苏诚盟装备股份有限公司 Polymer composite paper production equipment
CN115384075A (en) * 2022-08-29 2022-11-25 中化工程沧州冷却技术有限公司 Production process of filler for cooling tower

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