CN106514894A - Processing device for raw materials of plastic particles - Google Patents
Processing device for raw materials of plastic particles Download PDFInfo
- Publication number
- CN106514894A CN106514894A CN201611098989.XA CN201611098989A CN106514894A CN 106514894 A CN106514894 A CN 106514894A CN 201611098989 A CN201611098989 A CN 201611098989A CN 106514894 A CN106514894 A CN 106514894A
- Authority
- CN
- China
- Prior art keywords
- mixing chamber
- slide rail
- raw material
- pressing plate
- dryness storehouse
- 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.)
- Pending
Links
- 239000004033 plastic Substances 0.000 title claims abstract description 61
- 229920003023 plastic Polymers 0.000 title claims abstract description 61
- 239000002994 raw material Substances 0.000 title claims abstract description 31
- 239000002245 particle Substances 0.000 title abstract description 9
- 238000002156 mixing Methods 0.000 claims abstract description 59
- 239000000843 powder Substances 0.000 claims abstract description 57
- 238000003825 pressing Methods 0.000 claims abstract description 18
- 239000000463 material Substances 0.000 claims abstract description 11
- 238000010438 heat treatment Methods 0.000 claims description 12
- 238000007789 sealing Methods 0.000 claims description 5
- 230000032258 transport Effects 0.000 claims 1
- 239000000428 dust Substances 0.000 abstract description 7
- 238000001035 drying Methods 0.000 abstract 4
- 239000004594 Masterbatch (MB) Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000004140 cleaning Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000007921 spray Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000011812 mixed powder Substances 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000011265 semifinished product Substances 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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
- B29B13/00—Conditioning or physical treatment of the material to be shaped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/04—Cleaning involving contact with liquid
- B08B3/10—Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration
-
- 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
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/06—Conditioning or physical treatment of the material to be shaped by drying
- B29B13/065—Conditioning or physical treatment of the material to be shaped by drying of powder or pellets
-
- 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
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/10—Conditioning or physical treatment of the material to be shaped by grinding, e.g. by triturating; by sieving; by filtering
-
- 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
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/76—Mixers with stream-impingement mixing head
-
- 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
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/76—Mixers with stream-impingement mixing head
- B29B7/7631—Parts; Accessories
- B29B7/7636—Construction of the feed orifices, bores, ports
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The invention relates to the technical field of plastic particle processing, in particular to a processing device for raw materials of plastic particles. The processing device comprises a machine frame slidably connected with a slide rail; the slide rail is slidably connected with a sponge; a rinse tank and a drying bin are arranged below the slide rail; a rotary motor is further arranged above the drying bin; a cam is fixedly connected to the rotary motor; a transport pipe is connected to the lower end of the drying bin; one end of the transport pipe is connected with the drying bin, and the other end of the transport pipe is connected with a material mixing chamber of which the lower end is provided with a gas ejector pipe; a pressing plate for separating the material mixing chamber is horizontally arranged in the material mixing chamber and is slidably connected with the material mixing chamber; the lower end of the transport pipe is located in the position, below the pressing plate, of the side wall of the material mixing chamber; an operation rod is further fixedly connected to the upper end of the pressing plate; and the lower end of the operation rod is connected with a pressing rod, and the upper end of the operation rod penetrates through the upper end of the material mixing chamber and is connected with a hydraulic machine. According to the processing device for the raw materials of the plastic particles, a large amount of dust adsorbed by plastic powder can be cleaned up, the purity degree of finished plastic particles can be increased, and the raw materials can be mixed more uniformly.
Description
Technical field
The present invention relates to plastic grain processing technique field, more particularly, to a kind of plastic grain raw material disposal device.
Background technology
Plastic grain, is the semi-finished product of plastics processing industry, can be by continuing to be processed into the plastics systems such as polybag
Product.The raw material of processing plastic grain include plastic powders and for improving the antistatic master batch of plastics physical property, anti-stick
Even the powder materials such as masterbatch, pearly-lustre masterbatch, plastic powders are carried out being mixed by agitating device with various masterbatch powder materials, are mixed
Powder after conjunction is melted by way of heating, various raw material is fully merged.Afterwards, after being melted using extruder
Material be extruded into particle, just define after cooling required for plastic grain.
But, during storing to plastic powders, a certain amount of dust on plastic powders, can be stained with.Typically now not
Plastic powder to being adsorbed with dust is processed, but the plastic powders with dust are directly processed into plastic grain.This
Sample, can allow the plastic particle finished products for obtaining to have more impurity so that the quality of product is not pure enough.In addition, by stirring
When device is mixed, can there is the dead angle that agitating device cannot be contacted in mixing chamber all the time, so as to make the mixing of raw material inadequate
Uniformly.
The content of the invention
The invention is intended to provide a kind of plastic grain raw material disposal device, a large amount of ashes of plastic powders absorption can be removed
Dirt, improves the degree of purity of plastic particle finished products, additionally it is possible to make the mixing of raw material more uniform.
To achieve these goals, the present invention provides a kind of plastic grain raw material disposal device, including frame, in frame
Chute is vertically provided with, the slide rail being slidably connected with which in chute, is transversely provided with, sponge, one end of slide rail on slide rail, is slidably connected
Lower section is provided with rinse bath, and the dryness storehouse that top slidably connects sealing plate is provided with below the other end of slide rail, above dryness storehouse also
The rotary electric machine being fixedly connected with frame is provided with, the cam that convex portion is offseted with slide rail, dryness storehouse on rotary electric machine, is fixedly connected with
Lower end be connected with delivery tube, one end of delivery tube is connected with dryness storehouse, and the other end is connected with the batch mixing that lower end is provided with air jet pipe
Room, batch mixing indoor horizontal are provided with the pressing plate for separating mixing chamber, and pressing plate is slidably connected with mixing chamber madial wall, the lower end of delivery tube
On mixing chamber side wall below pressing plate, the upper end of pressing plate is also fixedly connected with action bars, and lower end and the pressing plate of action bars connect
Connect, the upper end of action bars passes through the upper end of mixing chamber and is connected with hydraulic press.
The know-why of the technical program and have the technical effect that：A kind of plastic grain raw material disposal device, by arranging
Rinse bath can be cleaned to plastic grain.As the density of plastic powders is less than the density of water in rinse bath, can float
Float on the surface, and the density of dust is typically larger than the density of water, can sink under water, so as to allow plastic powders to separate with dust.
Again because plastics now are in powder, with stronger surface tension, easily can be adsorbed onto on the material of porous.Cause
This, plastic powders are adsorbed from water by the technical program using sponge, and are dried in being transferred to dryness storehouse.In order to allow
Sponge adsorbs sponge in can reaching rinse bath, and slide rail is connected with housing slide so that slide rail can be with respect to moving down in frame
It is dynamic, so as to sponge can be moved up and down.
In order to plastic powders are separated from sponge, the technical program arranges the cam offseted with slide rail.Cam leads to
Rotary electric machine drive is crossed, during cam rotation, slide rail is ceaselessly clashed in the convex portion of cam, allows sponge constantly to vibrate, will
The plastic powders adsorbed on sponge are shaken off in dryness storehouse.
The technical program is provided with air jet pipe in the lower end of mixing chamber, can be passed through air always, in batch mixing in mixing chamber
Stable air-flow is formed in room.After various raw material powders enter mixing chamber, can constantly move in the presence of air-flow, from
And realize the mixing of different raw material.Mixed phase ratio is carried out using agitating device with prior art, air-flow can move to batch mixing
Each position of room, therefore, it is possible to avoid the appearance at batch mixing dead angle so that the mixing of raw material is more uniform.
After the completion of raw material mixing, by hydraulic press crush board sharp downward movement, increase the speed that powder is moved down,
Avoid causing the powder for eventually falling in mixing chamber bottom that layering occurs because of varying in weight for powder, cause powder mixing not uniform enough
Situation.
In sum, the technical program can realize the cleaning to plastic powders by arranging rinse bath, remove molding powder
The a large amount of dusts carried on end, make the plastic grain quality of shaping purer.In addition, batch mixing is carried out using air-flow by arranging
Mixing chamber, batch mixing dead angle can be eliminated so that the mixing of raw material is more uniform.
The following is the preferred version of such scheme：
Preferred version one：Based on base case, the side wall of the rinse bath is connected with air inlet pipe.It is passed through in rinse bath during cleaning
Air so that the water energy in rinse bath is enough rolled, and is rinsed to plastic powders so that cleaning is cleaner.
Preferred version two：Based on preferred version one, the side wall of the dryness storehouse is connected with steam heating pipe.By steam heating pipe to dry
70-80 ° of air is passed through in dry storehouse, powder is dried.In addition, the air being passed through can produce air-flow powder is dispelled,
It is more uniform that scattered powder can be mixed.
Preferred version three：Based on preferred version two, the side wall of the mixing chamber is provided with several charging apertures, connects on charging aperture
The powder sprinkler being connected to outside mixing chamber.Different raw material spray into mixing chamber from different powder sprinklers, and
And by arranging amount of powder and the ejection speed that powder sprinkler sprays, various raw material can be allowed to carry out according to certain ratio
Mixing.As the powder that sprinkler sprays is in scattered state, the powder therefore, it is possible to ensure different is reached after sprinkling
Mixed uniformly purpose.
Preferred version four：Based on preferred version three, the delivery tube in the shape of a spiral, powder along helix tube move with along straight line
Move downward and compare, because the tube wall with helix tube there occurs friction, therefore powder is lower into the speed of mixing chamber, so as to reduce
The impact force of powder and batch mixing chamber interior walls, it is to avoid mixing chamber is because being damaged by collision.
Preferred version five：Based on base case, the sponge upper end is fixedly connected with spring, and lower end and the sponge of spring connect
Connect, upper end and the slide rail of spring are slidably connected.Sponge is allowed to be connected with slide rail by spring so that sponge is because of knock over cam slide rail
While vibration, additionally it is possible to which that what is vibrated because of the elasticity of spring is fiercer, depart from the speed of sponge so as to accelerate plastic powders.
Preferred version six：Based on preferred version two, the steam heating pipe is fixedly connected with filter screen with the junction of dryness storehouse, filters
The filter opening aperture of net is 200-300 μm.During plastic powders are shaken off in sponge vibration, taken out from dryness storehouse using steam heating pipe
Gas so that the air pressure in dryness storehouse is dropped by less than atmospheric pressure, so as to form from dryness storehouse extroversion dryness storehouse the air-flow for moving, should
Air-flow can guide the plastic powders shaken off into dryness storehouse, it is to avoid plastic powders are moved to outside dryness storehouse in a large number, cause modeling
The waste at feed powder end.Further, since the particle diameter of plastic powders is typically larger than 300 μm, 300 μm are less than by arranging filter opening aperture
Filter screen, can avoid powder from being extracted out dryness storehouse by steam heating pipe.And when filter opening aperture is less than 200 μm, gas is difficult by quick
The filter screen, therefore the aperture of filter opening is also greater than 200 μm.
Description of the drawings
Structural representations of the Fig. 1 for the embodiment of the present invention.
Specific embodiment
Below by specific embodiment, the present invention is further detailed explanation：
Reference in Figure of description includes：Frame 1, slide rail 2, sponge 3, rinse bath 4, sealing plate 5, dryness storehouse 6, rotation
Motor 7, cam 8, delivery tube 9, air jet pipe 10, mixing chamber 11, pressing plate 12, action bars 13, hydraulic press 14, air inlet pipe 15, heating installation
Pipe 16, powder sprinkler 17.
The present embodiment is as shown in figure 1, plastic grain raw material disposal device, including vertically arranged frame 1, in frame 1
Vertically be provided with chute, chute is slidably connected with the slide rail 2 of horizontally set, on slide rail 2, also slidably connect sliding sleeve, slideway lower end with
One end of spring is fixedly connected, and the other end of spring is fixedly connected with the upper end of sponge 3.Rinse bath 4 is located under 2 one end of slide rail
Side, and is connected with air inlet pipe 15 on the side wall of rinse bath 4, dryness storehouse 6 is located at the lower section of 2 other end of slide rail, and dryness storehouse 6
Upper end is slidably connected with sealing plate 5.In addition, the side wall of dryness storehouse 6 is also connected with steam heating pipe 16, steam heating pipe 16 and dryness storehouse 6
Junction is fixedly connected with filter screen, 280 μm of the filter opening aperture of filter screen.The top of dryness storehouse 6 is additionally provided with what is be fixedly connected with frame 1
Rotary electric machine 7, rotating shaft and 8 interference fit of cam of rotary electric machine 7, and the convex portion of cam 8 can be offseted with slide rail 2.
The lower end of dryness storehouse 6 is fixedly connected with the upper end of delivery tube 9, delivery tube 9 in the shape of a spiral, and its lower end and mixing chamber
11 are fixedly connected, and the lower end of mixing chamber 11 is fixedly connected with air jet pipe 10.The side wall of mixing chamber 11 offers 3 charging apertures, often
Be respectively provided with during different 17,3 powder sprinklers 17 of powder sprinkler are respectively connected with individual charging aperture antistatic master batch,
Resist blocking and that masterbatch and pearly-lustre masterbatch.
Additionally, also level is provided with pressing plate 12 in mixing chamber 11, the end of pressing plate 12 is offseted with the side wall of mixing chamber 11, and
It is slidably connected with the inwall of mixing chamber 11.The upper end of pressing plate 12 is fixedly connected with the lower end of action bars 13, the upper end of action bars 13
It is fixedly connected through mixing chamber 11 with hydraulic press 14.
When the process of plastic powders is carried out using the present embodiment, plastic powders to be cleaned are poured into the cleaning for being marked with clear water
In groove 4, the air of a period of time is passed through in rinse bath 4 by air inlet pipe 15.Afterwards, one end time is stood, allows plastic powders
Separate with dust as far as possible.Allow slide rail 2 along 1 slide downward of frame again, plastic powders are adsorbed in the immersion clear water of sponge 3.It is complete
Sponge 3 into plastic powders absorption is moved with slide rail 2, and sponge 3 is moved to above dryness storehouse 6 along slide rail 2.Start and rotate electricity
Machine 7, allows cam 8 to rotate, and allows sponge 3 to vibrate by collision of 8 convex portion of cam with slide rail 2, and plastic powders are trembled into dryness storehouse 6
In.
After plastic powders enter dryness storehouse 6, mobile sealing plate 5 cuts out the upper end open of dryness storehouse 6, and passes through steam heating pipe 16
80 DEG C of air is passed through in dryness storehouse 6, plastic powders are disperseed and dried.The plastic powders dried are completed by spiral helicine
Delivery tube 9 is entered in mixing chamber 11, while spraying other raw material by powder sprinkler 17 in mixing chamber 11.By jet
Pipe 10 is passed through air in mixing chamber 11, forms constantly mobile air-flow, completes the mixing of raw material.After completing mixing, stop
The entrance of air, makes hydraulic press 14 rapidly moving downward with dynamic pressure plate 12, allows mixed-powder to be quickly moved to the bottom of mixing chamber 11
Portion.The raw material being well mixed just can be taken out afterwards from mixing chamber 11 carries out the processing of plastic grain.
Above-described is only embodiments of the invention, the known general knowledge here such as concrete structure and/or characteristic in scheme
Excessive description is not made.It should be pointed out that for a person skilled in the art, on the premise of without departing from present configuration, also
Some deformations and improvement can be made, these should also be considered as protection scope of the present invention, these are real all without the present invention is affected
The effect applied and practical applicability.This application claims protection domain should be defined by the content of its claim, specification
In specific embodiment etc. record the content that can be used for explaining claim.
Claims (7)
1. plastic grain raw material disposal device, it is characterised in that：Including frame, chute in frame, is vertically provided with, it is horizontal in chute
To the slide rail that is slidably connected with which is provided with, sponge is slidably connected on slide rail, rinse bath below one end of slide rail, is provided with, slide rail
The dryness storehouse that top slidably connects sealing plate is provided with below the other end, be additionally provided with above dryness storehouse be fixedly connected with frame turn
Dynamic motor, is fixedly connected with the cam that convex portion is offseted with slide rail on rotary electric machine, the lower end of dryness storehouse is connected with delivery tube, transports
One end of pipe is connected with dryness storehouse, and the other end is connected with the mixing chamber that lower end is provided with air jet pipe, and batch mixing indoor horizontal is provided with will be mixed
The pressing plate that material room separates, pressing plate are slidably connected with mixing chamber madial wall, and the lower end of delivery tube is located at the mixing chamber side below pressing plate
On wall, the upper end of pressing plate is also fixedly connected with action bars, and the lower end of action bars is connected with pressing plate, and the upper end of action bars passes through batch mixing
The upper end of room and it is connected with hydraulic press.
2. plastic grain raw material disposal device according to claim 1, it is characterised in that：The side wall of the rinse bath connects
It is connected to air inlet pipe.
3. plastic grain raw material disposal device according to claim 2, it is characterised in that：The side wall of the dryness storehouse connects
It is connected to steam heating pipe.
4. plastic grain raw material disposal device according to claim 3, it is characterised in that：The side wall of the mixing chamber sets
There are several charging apertures, the powder sprinkler being connected with charging aperture outside mixing chamber.
5. plastic grain raw material disposal device according to claim 4, it is characterised in that：The delivery tube is helically
Shape.
6. plastic grain raw material disposal device according to claim 1, it is characterised in that：The sponge upper end is fixed and is connected
Spring is connected to, the lower end of spring is connected with sponge, upper end and the slide rail of spring are slidably connected.
7. plastic grain raw material disposal device according to claim 3, it is characterised in that：The steam heating pipe and dryness storehouse
Junction be fixedly connected with filter screen, the filter opening aperture of filter screen is 200-300 μm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611098989.XA CN106514894A (en) | 2016-12-04 | 2016-12-04 | Processing device for raw materials of plastic particles |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611098989.XA CN106514894A (en) | 2016-12-04 | 2016-12-04 | Processing device for raw materials of plastic particles |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106514894A true CN106514894A (en) | 2017-03-22 |
Family
ID=58354461
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611098989.XA Pending CN106514894A (en) | 2016-12-04 | 2016-12-04 | Processing device for raw materials of plastic particles |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106514894A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107443626A (en) * | 2017-06-13 | 2017-12-08 | 东莞市汇如涞电能科技有限公司 | A kind of plastic grain charging device |
| CN108789917A (en) * | 2018-06-19 | 2018-11-13 | 惠州市中塑王塑胶制品有限公司 | A kind of plastic grain processing equipment |
| CN109249549A (en) * | 2018-10-29 | 2019-01-22 | 镇江亿维硅材料科技有限公司 | A kind of silicon rubber kneader |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1056503A (en) * | 1990-04-27 | 1991-11-27 | 日本触媒化学工业株式会社 | The continuous prilling process and the device thereof of super absorbent resin powder |
| CN2776654Y (en) * | 2005-03-07 | 2006-05-03 | 毕舒 | Composite modification device of powder |
| CN101406883A (en) * | 2007-10-08 | 2009-04-15 | 上海金发科技发展有限公司 | Device for separating powder on particle surface of plastic |
| CN101714590A (en) * | 2008-10-06 | 2010-05-26 | 珂琳21风险投资株式会社 | Method for producing semiconductor particles |
| CN101797561A (en) * | 2010-03-04 | 2010-08-11 | 宁海鑫城汽车配件有限公司 | Separation device of plastic particles and dust by negative-pressure air power |
| CN102416676A (en) * | 2011-12-21 | 2012-04-18 | 栾清杨 | Small plastic cleaning machine |
| CN204263406U (en) * | 2014-10-29 | 2015-04-15 | 广东亿捷科技发展有限公司 | A kind of waste plastics cleaning, dehydration, oven dry and dust removal integrated plant |
| CN204470081U (en) * | 2015-02-04 | 2015-07-15 | 马鞍山市科宏塑业科技实业发展有限公司 | Plastic pellet screening plant |
| CN104943022A (en) * | 2015-06-26 | 2015-09-30 | 天津鑫泰诺高分子科技有限公司 | Negative-pressure wind-power device for separating plastic granules and dust |
| CN204701024U (en) * | 2015-05-11 | 2015-10-14 | 孙立志 | A kind of impurity separating device for waste plastics recovery |
| CN206264199U (en) * | 2016-12-04 | 2017-06-20 | 重庆精榜高分子材料有限公司 | Plastic grain raw material disposal device |
-
2016
- 2016-12-04 CN CN201611098989.XA patent/CN106514894A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1056503A (en) * | 1990-04-27 | 1991-11-27 | 日本触媒化学工业株式会社 | The continuous prilling process and the device thereof of super absorbent resin powder |
| CN2776654Y (en) * | 2005-03-07 | 2006-05-03 | 毕舒 | Composite modification device of powder |
| CN101406883A (en) * | 2007-10-08 | 2009-04-15 | 上海金发科技发展有限公司 | Device for separating powder on particle surface of plastic |
| CN101714590A (en) * | 2008-10-06 | 2010-05-26 | 珂琳21风险投资株式会社 | Method for producing semiconductor particles |
| CN101797561A (en) * | 2010-03-04 | 2010-08-11 | 宁海鑫城汽车配件有限公司 | Separation device of plastic particles and dust by negative-pressure air power |
| CN102416676A (en) * | 2011-12-21 | 2012-04-18 | 栾清杨 | Small plastic cleaning machine |
| CN204263406U (en) * | 2014-10-29 | 2015-04-15 | 广东亿捷科技发展有限公司 | A kind of waste plastics cleaning, dehydration, oven dry and dust removal integrated plant |
| CN204470081U (en) * | 2015-02-04 | 2015-07-15 | 马鞍山市科宏塑业科技实业发展有限公司 | Plastic pellet screening plant |
| CN204701024U (en) * | 2015-05-11 | 2015-10-14 | 孙立志 | A kind of impurity separating device for waste plastics recovery |
| CN104943022A (en) * | 2015-06-26 | 2015-09-30 | 天津鑫泰诺高分子科技有限公司 | Negative-pressure wind-power device for separating plastic granules and dust |
| CN206264199U (en) * | 2016-12-04 | 2017-06-20 | 重庆精榜高分子材料有限公司 | Plastic grain raw material disposal device |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107443626A (en) * | 2017-06-13 | 2017-12-08 | 东莞市汇如涞电能科技有限公司 | A kind of plastic grain charging device |
| CN107443626B (en) * | 2017-06-13 | 2019-12-20 | 东莞市汇如涞电能科技有限公司 | Plastic granules throws material device |
| CN108789917A (en) * | 2018-06-19 | 2018-11-13 | 惠州市中塑王塑胶制品有限公司 | A kind of plastic grain processing equipment |
| CN109249549A (en) * | 2018-10-29 | 2019-01-22 | 镇江亿维硅材料科技有限公司 | A kind of silicon rubber kneader |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206264199U (en) | Plastic grain raw material disposal device | |
| CN106514894A (en) | Processing device for raw materials of plastic particles | |
| CN212045477U (en) | Plastic particle filtering and dust removing device | |
| CN209222600U (en) | A kind of tea screening device | |
| CN207872676U (en) | A kind of plastic grain hierarchy system | |
| CN207025920U (en) | A kind of die surface dust cleaning plant | |
| CN203886787U (en) | Particle material screening machine | |
| CN210732923U (en) | Plastic powder dust collector | |
| CN108297308B (en) | Technics of reclaim of plastic waste device | |
| CN108148694B (en) | Soap processing method | |
| CN205731986U (en) | A kind of plastic pellet dust removal by filtration device | |
| CN109107641A (en) | A kind of energy-saving food processing rice cleaning device | |
| CN112246603A (en) | Sieving mechanism is used in industrial chemicals processing | |
| CN209061254U (en) | A kind of chemical industry grinding device | |
| CN215242121U (en) | Dust removal discharging device for plastic particle processing | |
| CN110281410A (en) | A kind of Wood plastic composite production raw material proportioning equipment | |
| CN217318748U (en) | Plastic granulating device for plastic granulator | |
| CN206435479U (en) | A kind of catalyst wet material separating device | |
| CN205799935U (en) | A kind of plastic pellet filtration drying all-in-one | |
| CN214894390U (en) | Soil sample preparation all-in-one | |
| CN109591216B (en) | Feeding device for injection mold | |
| CN104475338A (en) | Air separation impurity remover | |
| CN211307030U (en) | Plastic granulator | |
| CN211054383U (en) | Drying device of plastic extruder | |
| CN211027061U (en) | Pesticide powder sieving machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170322 |