CN107379317A - A kind of ultra-fine level multicomponent Tissuemat E granulating production equipment - Google Patents
A kind of ultra-fine level multicomponent Tissuemat E granulating production equipment Download PDFInfo
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- CN107379317A CN107379317A CN201710754503.1A CN201710754503A CN107379317A CN 107379317 A CN107379317 A CN 107379317A CN 201710754503 A CN201710754503 A CN 201710754503A CN 107379317 A CN107379317 A CN 107379317A
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- China
- Prior art keywords
- top cover
- atomization
- tank
- tissuemat
- ultra
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- 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.)
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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
- B29B9/00—Making granules
- B29B9/10—Making granules by moulding the material, i.e. treating it in the molten state
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/04—Polymers of ethylene
- B29K2023/06—PE, i.e. polyethylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2091/00—Use of waxes as moulding material
Abstract
A kind of ultra-fine level multicomponent Tissuemat E granulating production equipment, including mixing device, insulation conveyance conduit and atomization granulating apparatus；Mixing device includes the mixing tank being made up of inner and outer shell, the clip cavity of storage heating oil is formed between two housings, the top of mixing tank is equipped with the top cover A with material inlet, batch mixing motor is installed on top cover A, it exports axis connection puddle support, and the bottom position of mixing tank is provided with mixed material discharge conection；Atomization granulating apparatus includes atomization tank, top is equipped with top cover B, equipped with atomization disk-drive motor on top cover B, it exports axis connection atomizing disk, the inner mixed material input adapter for extending to atomizing disk input port is coated with top cover B, the bottom of atomization tank is wax grain delivery outlet, and atomization tank is connected with air draught cooling structure；The input and mixed material discharge conection for being incubated conveyance conduit are tightly connected, and the boosted pump of output end and the outer end of mixed material input adapter are tightly connected.This equipment production wax grain component uniformly, granularity uniformity it is good.
Description
Technical field
The invention belongs to ultra-fine grade PVC wax powder production technical field, more particularly to a kind of ultra-fine poly- second of level multicomponent
Alkene wax grain production equipment.
Background technology
Polyethylene wax powder is also known as macromolecule wax, abbreviation Tissuemat E.It has excellent cold resistance, heat resistance, chemically-resistant
Property and wearability, make Tissuemat E be widely used in manufacture Masterbatch, granulation, plastic-steel, PVC, PUR, rubber, shoe polish,
The products such as leather gloss agent, cable insulating material, floor wax, plastic material, ink, injection.Tissuemat E is more in the form of wax powder
Applied in product, wax powder is thinner better with the major constituent combination effect of product.
At present, producing the mode of polyethylene wax powder has a variety of, mainly there is swing crushing method, spray-on process, air-flow grinding method etc.,
In addition, Application No. 201510153589.3, entitled：A kind of process for preparing Tissuemat E grinding, discloses one kind
Utilize the method that grinding production is realized using super-critical rapid expansion technology.
The method of existing a variety of production polyethylene wax powders is by processing Tissuemat E by Tissuemat E grain raw material
Powder, for the polyethylene wax powder that product is one pack system, existing production method and production equipment can meet production requirement substantially, and
It is multi-component polyethylene wax powder for product, in production, usually mixes Tissuemat E grain raw material with other raw materials, altogether
At progress efflorescence, and there is the problem of component skewness in the multicomponent polyethylene wax powder so produced.
To ensure the uniformity of the component of multicomponent polyethylene wax powder, best solution method is：Tissuemat E grain raw material
To contain multi-component Tissuemat E grain.Therefore, it is necessary to develop the granulating production equipment of a set of multicomponent Tissuemat E.
The content of the invention
The Tissuemat E grain component that the present invention provides a kind of production for technical problem present in solution known technology is equal
Ultra-fine level multicomponent Tissuemat E granulating production equipment even, granularity uniformity is good.
The present invention is adopted the technical scheme that to solve technical problem present in known technology：
A kind of ultra-fine level multicomponent Tissuemat E granulating production equipment, it is characterised in that：Including mixing device, insulation conveying
Pipeline and atomization granulating apparatus；
The mixing device includes mixing tank, and mixing tank is connected and composed by inner housing and shell body, between inner and outer shell
The clip cavity for storing heating oil is formed, electrical heating elements are provided with clip cavity, top cover A is installed at the top of mixing tank,
Material inlet is offered on top cover A, batch mixing motor is installed on top cover A, the output shaft of batch mixing motor passes through
Top cover A is extend into mixing tank, and the puddle support drive connection with being arranged in mixing tank；Installed in the bottom position of mixing tank
There is mixed material discharge conection；
The atomization granulating apparatus includes atomization tank, is provided with top cover B at the top of atomization tank, mist is provided with top cover B
Change disk-drive motor, the output shaft for being atomized disk-drive motor is extend into atomization tank through top cover B and with being arranged in atomization tank
Atomizing disk drive connection, mixed material input adapter, the inner extension of mixed material input adapter are also coated with top cover B
To the input port position of atomizing disk；Wax grain delivery outlet is formed on the bottom of atomization tank, and discharging gear door is provided with wax grain equipped at outlet port,
Position on top cover B or on atomization tank close to top is provided with exhaust port, and the air-suction duct of exhaust port and peripheral hardware connects,
Air-suction duct connects air-introduced machine, forms air draught cooling structure；
The input and mixed material discharge conection for being incubated conveyance conduit are tightly connected, and are incubated the output end warp of conveyance conduit
Elevator pump and the outer end of mixed material input adapter are tightly connected.
Further：It is described insulation conveyance conduit by the inner tube for conveying liquefied mixture material, be set in outside inner tube
Outer tube and be coated and fixed outside pipe outer thermal insulation layer composition；The both ends of inner tube form the input of insulation conveyance conduit respectively
With the output end of insulation conveyance conduit, said inner tube uses high thermal conductive metallic pipe；The both ends of outer tube respectively pass through end plate and inner tube
Closing connection is formed, makes to form the toroidal cavity for conveying heating oil between inner tube and outer tube, close to both ends on outer tube
Position is respectively arranged with the oily input interface of heating and heats oily output interface, heats oily input interface and heats oily output interface and leads to
External pipeline is crossed to be connected with heat cycles device.
More further：The helical form deflector for moving towards arrangement along pipeline is installed in toroidal cavity, makes annular
Cavity forms helical form flow-guiding channel chamber.
Further：The outer thermal insulation layer uses aeroge compound heat-insulation felt, the outer thermal insulation layer by article tape or
Band wrapping is fixed on outer tube.
Further：The puddle support stirs the multiple stirrings of frame and welding machine on two vertical edges of stirring frame by rectangle
Bar is formed, and puddler, which is presented, to be obliquely installed.
Further：The oily grouting socket pipe of heating is installed close to the position at top on shell body, in heating oil injection
The outer end of mouthpiece is provided with controlled valve.
The present invention has the advantages and positive effects of：
This granulating production equipment makes several material components realize uniform mixing, mixing under liquid condition by mixing device
Homogeneous material afterwards is thrown away, in matching somebody with somebody for air draught cooling structure by insulation delivery pipe being delivered to granulating apparatus by atomizing disk
Under cooperation is used, atomization production polyethylene wax material.The Tissuemat E grain component produced by this granulating production equipment is uniform, granularity one
Cause property is good.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention；
Fig. 2 is the structural representation that conveyance conduit is incubated in Fig. 1.
In figure：1st, mixing device；1-1, mixing tank；1-1-1, inner housing；1-1-2, shell body；1-1-3, clip cavity；1-2、
Electrical heating elements；1-3, top cover A；1-3-1, material inlet；1-4, batch mixing motor；1-5, puddle support；1-5-1, rectangle stir
Mix frame；1-5-2, puddler；1-6, mixed material discharge conection；1-7, the oily grouting socket pipe of heating；1-8, controlled valve；2nd, protect
Warm conveyance conduit；2-1, inner tube；2-1-1, input；2-1-2, output end；2-2, outer tube；2-2-1, the oily input interface of heating；
2-2-2, the oily output interface of heating；2-3, outer thermal insulation layer；2-4, toroidal cavity；2-5, helical form deflector；3rd, it is atomized granulating dress
Put；3-1, atomization tank；3-2, top cover B；3-3, atomization disk-drive motor；3-4, atomizing disk；3-5, mixed material input adapter；3-
6th, discharging gear door；3-7, exhaust port；3-8, air-suction duct；3-9, air-introduced machine；4th, elevator pump.
Embodiment
In order to further understand the content, features and effects of the present invention, hereby enumerating following examples, and coordinate accompanying drawing
Describe in detail as follows：
Fig. 1-2, a kind of ultra-fine level multicomponent Tissuemat E granulating production equipment are referred to, its innovative point is：Including mixed
Expect device 1, insulation conveyance conduit 2 and atomization granulating apparatus 3.Insulation conveyance conduit is used to connect mixing device and atomization granulating dress
Put, realize the conveying of liquefied mixture material, avoid liquefied mixture material during conveying, realized in insulation conveyance conduit
Solidification.
The mixing device includes mixing tank 1-1, and mixing tank is connected and composed by inner housing 1-1-1 and shell body 1-1-2.
The clip cavity 1-1-3 for storing heating oil is formed between inner and outer shell, electrical heating elements 1-2, electrical heating are provided with clip cavity
Element can use common heating tube or heating rod structure, and the quantity and set location of electrical heating elements are added with that can realize that oil is uniform
Heat and be easy to electric wire draw be advisable.Top cover A1-3 is installed at the top of mixing tank, material inlet 1- is offered on top cover A
3-1.Batch mixing motor 1-4 is installed on top cover A, the output shaft of batch mixing motor extend into mixing tank through top cover A
It is interior, and the puddle support 1-5 drive connections with being arranged in mixing tank.Mixed material output is installed in the bottom position of mixing tank
Adapter 1-6.
The atomization granulating apparatus includes atomization tank 3-1, is provided with top cover B3-2 at the top of atomization tank, pacifies on top cover B
Equipped with atomization disk-drive motor 3-3, be atomized the output shaft of disk-drive motor through top cover B extend into atomization tank it is interior and with setting
Atomizing disk 3-4 drive connections in atomization tank, are also coated with mixed material input adapter 3-5 on top cover B, and mixed material is defeated
The inner for entering adapter extends to the input port position of atomizing disk；Wax grain delivery outlet is formed on the bottom of atomization tank, in wax grain delivery outlet
Place is provided with discharging gear door 3-6, and in granulation process is atomized, discharging gear door is closed, and is formed with wax grain delivery outlet close
Envelope, after the wax grain generated in atomization tank reaches set amount, discharging gear door is opened, wax grain is exported, to realize that subsequent granulation is given birth to
Production.Discharging gear door can be arranged on wax grain equipped at outlet port using various ways, such as, one end and the atomization pot bottom of discharging gear door
One side is attached using articulated manner, is set between the other end of discharging gear door and the opposite side position of atomization pot bottom
Manual high-speed switch mechanism, manually high-speed switch mechanism, which realizes to discharge, keeps off the opening and closing locking of door.On top cover B or
Position on atomization tank close to top is provided with exhaust port 3-7, the air-suction duct 3-8 connections of exhaust port and peripheral hardware, air draught
Pipeline connects air-introduced machine 3-9, forms air draught cooling structure, to realize that the wax thrown away from atomizing disk solidifies during dropping in whereabouts
Granulating.
The input and mixed material discharge conection for being incubated conveyance conduit are tightly connected, and are incubated the output end warp of conveyance conduit
Elevator pump 4 and the outer end of mixed material input adapter are tightly connected.
Above-mentioned insulation conveyance conduit further uses following structure：
The insulation conveyance conduit is by inner tube 2-1, the outer tube 2-2 being set in outside inner tube for conveying liquefied mixture material
And the outer thermal insulation layer 2-3 compositions in outside pipe are coated and fixed.The both ends of inner tube form the input of insulation conveyance conduit respectively
2-1-1 and insulation conveyance conduit output end 2-1-2, said inner tube use high thermal conductive metallic pipe.The both ends of outer tube respectively pass through
End plate forms closing connection with inner tube, makes to form the toroidal cavity 2-4 for conveying heating oil between inner tube and outer tube, in outer tube
The upper position close to both ends is respectively arranged with the oily input interface 2-2-1 of heating and heats oily output interface 2-2-2, heats oil input
Interface and the oily output interface of heating are connected by external pipeline with heat cycles device, and wherein external pipeline and heat cycles pump exists
Not shown in accompanying drawing.
In above-mentioned insulation conveyance conduit, the spiral for moving towards arrangement along pipeline is further fitted with toroidal cavity
Shape deflector 2-5, make toroidal cavity formed helical form flow-guiding channel chamber, so, can make heating oil in toroidal cavity helically
Shape flow regime, make even heat passes to the mixed material conveyed in inner tube.
In above-mentioned insulation conveyance conduit：The outer thermal insulation layer uses aeroge compound heat-insulation felt, and the outer thermal insulation layer leads to
Cross article tape or band wrapping is fixed on outer tube.
The above-mentioned further preferred structure of puddle support is：The puddle support stirs frame 1-5-1 and welding machine in stirring frame by rectangle
Two vertical edges on multiple puddler 1-5-2 form, puddler, which is presented, to be obliquely installed.The puddle support structure can reach larger
Agitation area, further, it may have larger endurance.
Position close to top on the shell body of above-mentioned outer mixing tank is further fitted with heating oily grouting socket pipe 1-
7, controlled valve 1-8 is installed in the outer end for heating oily grouting socket pipe, sets the oily grouting socket pipe of heating to facilitate heating oil
Injection and supplement.
Various ingredients are first stirred by this ultra-fine level multicomponent Tissuemat E granulating production equipment under heating environment, are made
Various ingredients realize uniformly mixing, are then delivered in the atomization tank of atomization granulating apparatus, are being atomized by being incubated conveyance conduit
Tank intrinsic fog is melted into Tissuemat E grain, so as to ensure that being uniformly distributed for Tissuemat E grain component, and then ensure that subsequently through poly-
When ethylene waxes grain produces polyethylene wax powder, each component is uniformly distributed in wax powder.
Claims (6)
- A kind of 1. ultra-fine level multicomponent Tissuemat E granulating production equipment, it is characterised in that：Including mixing device, insulation delivery pipe Road and atomization granulating apparatus；The mixing device includes mixing tank, and mixing tank is connected and composed by inner housing and shell body, formed between inner and outer shell For storing the clip cavity of heating oil, electrical heating elements are provided with clip cavity, top cover A is installed at the top of mixing tank, are being pushed up Material inlet is offered on lid A, batch mixing motor is installed on top cover A, the output shaft of batch mixing motor passes through top cover A It extend into mixing tank, and the puddle support drive connection with being arranged in mixing tank；It is provided with the bottom position of mixing tank mixed Compound material discharge conection；The atomization granulating apparatus includes atomization tank, is provided with top cover B at the top of atomization tank, atomizing disk is provided with top cover B Motor, it is atomized the output shaft of disk-drive motor and is extend into through top cover B in atomization tank and the mist with being arranged in atomization tank Change dish driving connection, mixed material input adapter is also coated with top cover B, the inner of mixed material input adapter extends to mist Change the input port position of disk；Wax grain delivery outlet is formed on the bottom of atomization tank, is provided with discharging gear door in wax grain equipped at outlet port, is pushing up Exhaust port, the air-suction duct connection of exhaust port and peripheral hardware, air draught are provided with lid B or close to the position at top on atomization tank Pipeline connects air-introduced machine, forms air draught cooling structure；The input and mixed material discharge conection for being incubated conveyance conduit are tightly connected, and the output end for being incubated conveyance conduit is boosted Pump and the outer end of mixed material input adapter are tightly connected.
- 2. ultra-fine level multicomponent Tissuemat E granulating production equipment according to claim 1, it is characterised in that：The insulation Conveyance conduit is by the inner tube for conveying liquefied mixture material, the outer tube being set in outside inner tube and is coated and fixed in outside pipe Outer thermal insulation layer is formed；The both ends of inner tube form the input of insulation conveyance conduit and the output end of insulation conveyance conduit, institute respectively State inner tube and use high thermal conductive metallic pipe；The both ends of outer tube respectively form closing connection by end plate and inner tube, make inner tube and outer tube Between formed for convey heating oil toroidal cavity, on outer tube close to both ends position be respectively arranged with heating oil input connect Mouth and the oily output interface of heating, heat oily input interface and the oily output interface of heating passes through external pipeline and heat cycles device company Connect.
- 3. ultra-fine level multicomponent Tissuemat E granulating production equipment according to claim 2, it is characterised in that：Annular empty Intracavitary is provided with the helical form deflector for moving towards arrangement along pipeline, toroidal cavity is formed helical form flow-guiding channel chamber.
- 4. ultra-fine level multicomponent Tissuemat E granulating production equipment according to claim 2, it is characterised in that：It is described it is outer every Thermosphere uses aeroge compound heat-insulation felt, and the outer thermal insulation layer is fixed on outer tube by article tape or band wrapping.
- 5. ultra-fine level multicomponent Tissuemat E granulating production equipment according to claim 1, it is characterised in that：The stirring Frame stirs the multiple puddlers of frame and welding machine on two vertical edges of stirring frame by rectangle and formed, and puddler is presented inclination and set Put.
- 6. ultra-fine level multicomponent Tissuemat E granulating production equipment according to claim 1, it is characterised in that：In shell body The upper position close to top is provided with the oily grouting socket pipe of heating, and switch valve is provided with the outer end for heating oily grouting socket pipe Door.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710754503.1A CN107379317A (en) | 2017-08-29 | 2017-08-29 | A kind of ultra-fine level multicomponent Tissuemat E granulating production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710754503.1A CN107379317A (en) | 2017-08-29 | 2017-08-29 | A kind of ultra-fine level multicomponent Tissuemat E granulating production equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107379317A true CN107379317A (en) | 2017-11-24 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710754503.1A Pending CN107379317A (en) | 2017-08-29 | 2017-08-29 | A kind of ultra-fine level multicomponent Tissuemat E granulating production equipment |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6238732B1 (en) * | 1996-11-18 | 2001-05-29 | H. B. Fuller Licensing & Financing Inc. | Method for making hot melt adhesive pellet comprising continuous coating of pelletizing aid |
| CN1974645A (en) * | 2006-12-08 | 2007-06-06 | 郑州市腾飞实业有限责任公司 | Completely biodegradable plastic |
| CN103275335A (en) * | 2013-05-20 | 2013-09-04 | 安徽理工大学 | Preparation method of polyethylene wax micropowder and spray granulation system |
| CN205308206U (en) * | 2016-01-19 | 2016-06-15 | 广州立之力机械设备有限公司 | Energy -efficient agitator tank |
| CN205579160U (en) * | 2016-04-20 | 2016-09-14 | 东莞三江港口储罐有限公司 | Dangerous chemical liquid pipeline system with constant temperature function |
| CN206285911U (en) * | 2016-12-09 | 2017-06-30 | 青岛赛诺新材料有限公司 | The special adjustable multifunctional spray shaping tower of production Tissuemat E |
-
2017
- 2017-08-29 CN CN201710754503.1A patent/CN107379317A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6238732B1 (en) * | 1996-11-18 | 2001-05-29 | H. B. Fuller Licensing & Financing Inc. | Method for making hot melt adhesive pellet comprising continuous coating of pelletizing aid |
| CN1974645A (en) * | 2006-12-08 | 2007-06-06 | 郑州市腾飞实业有限责任公司 | Completely biodegradable plastic |
| CN103275335A (en) * | 2013-05-20 | 2013-09-04 | 安徽理工大学 | Preparation method of polyethylene wax micropowder and spray granulation system |
| CN205308206U (en) * | 2016-01-19 | 2016-06-15 | 广州立之力机械设备有限公司 | Energy -efficient agitator tank |
| CN205579160U (en) * | 2016-04-20 | 2016-09-14 | 东莞三江港口储罐有限公司 | Dangerous chemical liquid pipeline system with constant temperature function |
| CN206285911U (en) * | 2016-12-09 | 2017-06-30 | 青岛赛诺新材料有限公司 | The special adjustable multifunctional spray shaping tower of production Tissuemat E |
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