CN200998656Y - Feeding mechanism of pelletizer - Google Patents

Feeding mechanism of pelletizer Download PDF

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Publication number
CN200998656Y
CN200998656Y CNU2007201060005U CN200720106000U CN200998656Y CN 200998656 Y CN200998656 Y CN 200998656Y CN U2007201060005 U CNU2007201060005 U CN U2007201060005U CN 200720106000 U CN200720106000 U CN 200720106000U CN 200998656 Y CN200998656 Y CN 200998656Y
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CN
China
Prior art keywords
spiral
blade
rotating shaft
central rotating
section
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.)
Expired - Fee Related
Application number
CNU2007201060005U
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Chinese (zh)
Inventor
叶仕超
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yuyao Lvdao Plastic & Rubber Machinery Co Ltd
Original Assignee
Yuyao Lvdao Plastic & Rubber Machinery Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
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Application filed by Yuyao Lvdao Plastic & Rubber Machinery Co Ltd filed Critical Yuyao Lvdao Plastic & Rubber Machinery Co Ltd
Priority to CNU2007201060005U priority Critical patent/CN200998656Y/en
Application granted granted Critical
Publication of CN200998656Y publication Critical patent/CN200998656Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a feeding mechanism of a pelleting machine. Material crushed through a crushing machine is delivered into a feeding bucket provided with an inductor through a conveying pipeline system, and the material entering into the feeding bucket is conveyed to a main machine screw rod through a stirring mechanism. The stirring mechanism is composed of a stirring section and a pressurizing conveying section; wherein the stirring section is a material stirring rod installed at the upper section of a central rotary shaft, and the pressurizing conveying section is a structure that a material stirring rod installed at the lower section of the central rotary shaft is matched with a spiral blade. The spiral blade is composed of a spiral spreading blade and a standard spiral pressurizing piece positioned on the lower surface of the spiral spreading blade; the front end of the standard spiral pressurizing piece adopts a dual-spiral structure. The utility model has the advantages of reasonable structure, simple operation, uniform running, stability and reliability, and high extrusion palletizing efficiency, the reduction of production cost, and the saving of energy consumption.

Description

The feeding mechanism of comminutor
Technical field
The utility model relates to a kind of plastic granulating equipment, relates in particular to the feeding mechanism that a kind of film, waste silk and sheet stock reclaim plastic granulating equipment.
Background technology
Reclaimed materials such as the film of prior art, waste silk and sheet stock add the technology complexity, and granulation efficiency is low, the production cost height.In order to simplify production technology, to enhance productivity, the research of molding machine industry and production unit have proposed new design one after another.As Chinese patent CN88270670U membranaceous waste or used plastics wet feed extruding and granulating equipment, adopt at least two be cascaded equidistant not wait dark screw extruder, wherein first is the drainage type extruder, last platform machine is the bleeder extruder; Be connected with the sealing adaptor elbow with the inclined-plane die head between the two extruders, and the reinforced roll-type feeding device that adopts, filter screen adopts manual inclined plane ring structure to be connected with fervent die head.Above-mentioned patent adopts two extruders, and production cost and energy consumption are higher, and efficient is on the low side.
Summary of the invention
Main purpose of the present utility model is to solve the existing in prior technology technical problem, thereby develops a kind of raising extruding pelletization efficient, reduces production costs the feeding mechanism of the comminutor that energy savings consumes.
Another purpose of the present utility model is: improve the granulation quality, guarantee that the particle size of creating is even, the feeding mechanism of full and glossiness plastic granulator.
Technical problem of the present utility model is mainly solved by following technical proposals: a kind of comminutor feeding mechanism, send into the head tank that inductor is housed through pipeline system by the material that pulverizer is pulverized, the material that enters head tank is delivered to main-machine screw by rabbling mechanism, it is characterized in that: described rabbling mechanism is formed by stirring section and pressurized delivered section; Describedly stir the spice bar that section is mounted in the central rotating shaft epimere, the spice bar that described pressurized delivered section is mounted in the central rotating shaft hypomere and spiral launch blade and the master screw of spice bar below being positioned at spiral expansion blade and add the compressing tablet structure that matches.Gap between described helical blade and the head tank bucket wall is between 10~70mm.The spindle nose end of described central rotating shaft and main-machine screw distance are between 20~70mm.
The technical solution of the utility model can also be further perfect,
As preferably, the spiral external diameter that described master screw adds compressing tablet is 1: 1.2~1: 2 of main-machine screw length; Pitch be master screw add the compressing tablet diameter 1/2~3/4; Master screw adds compressing tablet around the pitch of central rotating shaft total length at 2~3 times.
As preferably, described master screw adds the front end of compressing tablet around central rotating shaft, that is: about 1/4 spiral adopts double helix; The parameter of the helical blade that described double helix increased is identical with former helical blade, is connected former helical blade symmetric position in the same way.The front end of central rotating shaft radially adds compressing tablet original position 180 degree of being separated by with the master screw of former main body, and effect is to increase downward pressure frequency.
As preferably, described spice bar by spiral launch direction blade become 120 ° spaced apart around central rotating shaft.First spice bar should be chosen in terminal shaft that master screw adds compressing tablet to downward half pitch, in the middle of the just terminal downward pitch.Spice bar and head tank bucket wall gap are 15~30mm, decide according to the size of overall system and the material that is suitable for.The need of the long 150mm of surpassing of spice bar are done welding and are strengthened.
The beneficial effects of the utility model are: said device features rational structure, and easy and simple to handle, operation is even, steady, reliable, and extruding pelletization efficient height has reduced production cost, energy savings consumption.And make the plastic pellet size of creating evenly full and glossy, solve that film, waste silk and sheet stock organic efficiency are low for many years, reclaim to add the technology complicated situation.
Description of drawings
Accompanying drawing 1 is a kind of system architecture schematic diagram of the present utility model;
Accompanying drawing 2 is rabbling mechanism enlarged drawings of Fig. 1.
The specific embodiment
Below by embodiment, and in conjunction with the accompanying drawings, the technical scheme of inventing is further described in detail.
Shown in Fig. 1 Fig. 2 showed, pulverizer 1 entered head tank 14 by conveying fan 2, conveyance conduit 3, cyclone separator 4, linked to each other with connecting flange 5 between cyclone separator 4 and the head tank 14.The lower end of head tank 14 links to each other with the main frame barrel 11 that main-machine screw 10 is installed by main frame barrel flange 12, and main-machine screw 10 links to each other with main frame gear reduction box 22 on being installed in main frame shelf 23 and by electric cabinet 24 controls.Head tank 14 is installed in to be installed on the shelf 21, and the staving of head tank 14 is equipped with upper infrared inductor 15 and the next infrared inductor 13.Central rotating shaft 7 is equipped with in the centre of head tank 14, central rotating shaft 7 be installed in buncher, motor pulley, reductor belt pulley 18, cycloid speed reducer 17, the central rotating shaft fixed screw 16 installed on the shelf and be connected.Epimere at central rotating shaft 7 is equipped with spice bar 6, and hypomere is equipped with spice bar 6 and adds spice and the pressurized delivered mechanism that compressing tablet 9 combines with spiral expansion blade 8 and master screw.Match with main-machine screw 10 in the end of central rotating shaft 7.
Below main inventive point of the present utility model is set forth:
1, pulverizer 1: adopt special stationary knife herringbone design, cutting knife is one group of a slice, and parallel installation reduces cutting and impacts, and cutting stress is disperseed to make installation, gap adjustment and the regular maintenance of cutting knife stable rotation the convenience again simultaneously blade to both sides.Charging aperture has been done the increasing design, and discharge bucket adopts material collection and the conveying after the design of wind collection formula makes things convenient for blower fan connection and pulverizing.
2, conveying fan 2: done improvement on the basis of centrifugal blower, the air intake angle is amplified and blast pipe directly connects with the pulverizer discharge bucket, and the corresponding amplification of wind pipe reaches the effect of the incremental amount of decompression power, and the big noise of conveying capacity is relatively low.
3, conveyance conduit 3: adopt in the PE material conveyance conduit with the spiral reinforcement of steel wire, intensity height, easy for installation and can not produce the characteristics of noise.
4, cyclone separator 4: will be separated with the mixture of material by the air stream that pipeline enters, material is sent in head tank 14, air is discharged to reach effective separation purpose from central tube.
5, connecting flange 5: make taper design, last bore is identical with cyclone separator 4 outlets, following bore identical with head tank 14 openings (littler) than last bore, the tapering size is suitable with cyclone separator 4 lower body rotary wind sections, reaches not increase the purpose that device height makes things convenient for installation and maintenance again when prolonging the separator lower body.
6, spice bar 6: be divided into two parts up and down on function is used: spiral launches the part of blade more than 8 and is referred to as top, mainly be to mix the material in the head tank 14 4 blankings of thoroughly convenient branch cyclone separator, also, material launches blade 8 when mixing thoroughly for evenly entering spiral downwards, spiral launches the following part of blade and is referred to as the lower part, mainly be to add compressing tablet 9 with spiral expansion blade 8 and master screw to be used, when main-machine screw 10 inlet amounies are launched blade 8 and master screw when adding compressing tablet 9 feeding coals less than spiral, material will be compacted, the resistance that central shaft 7 rotation spirals expansion blades and master screw add compressing tablet increases exponentially, the latter half spice bar is mixed material under this situation, partial material can upwards play anti-material effect, does not destroy drive disk assembly to such an extent as to whole like this charging system resistance just can not increase exponentially, motor, head tank, spiral launches blade and central shaft etc.Spice bar 6 adopts with central rotating shaft 7 and is welded to connect, first spice bar should be chosen in master screw and add the terminal shaft of compressing tablet to downward half pitch (in the middle of the just terminal downward pitch), spice bar 6 is afterwards pressed spiral expansion blade 8 directions (equidirectional with spiral expansion blade) and is become 120 degree spaced apart around central rotating shaft 7, and spice bar 6 is 15~30mm (deciding according to the size of overall system and the material that is suitable for) with charging staving 14 gaps.The need of the long 150mm of surpassing of spice bar are done welding and are strengthened.
7, central rotating shaft 7: provide moment for spice bar 6, spiral expansion blade 8 and master screw add compressing tablet 9 in reinforced process.Spindle nose end and main-machine screw 10 distances should remain within 20~70mm during design and installation, and definite distance should be according to material and variant.
8, spiral launches blade 8: be used to collect the material that evenly gets off from top spice bar 6 and carry out once spiral downward extruding, make material density increase to following master screw to a certain extent and add compressing tablet 9 chargings and prepare.The shape that spiral launches blade 8 becomes spiral expansion, adopts electric welding to connect with central rotating shaft, during design and installation and head tank should stay gap, 3~5cm left and right sides so that instead when material pressure is excessive expect.
9, master screw adds compressing tablet 9: in close relations with main-machine screw conveying capacity and material situation, the spiral external diameter becomes 1: 1.2 with main-machine screw~and 1: 2 ratio makes, pitch be diameter 1/2~3/4 between, master screw adds compressing tablet will be 2~3 times pitch around the central rotating shaft total length.The front end (also being the front end of central rotating shaft) that adds compressing tablet 9 at master screw adopt double helix, a spiral plate (structural parameters that add compressing tablet with original master screw are identical) of adding up generally have only around the spiral of central rotating shaft about 1/4 and former spiral be welded in the same way symmetric position (front end of central rotating shaft radially with the master screw of former main body add the compressing tablet original position be separated by 180 spend).Effect is to increase downward pressure frequency, even charging and make the pressure balance in the reinforced process in order to avoid make the monolateral stressed generation skew of central shaft, head tank wiped by compressing tablet or main frame barrel flange produces damaged phenomenon, and serious meeting makes the central rotating shaft distortion or twists off.When master screw adds the compressing tablet design and installation and head tank should stay gap, 10~20mm left and right sides so that install and use.
10, the next infrared inductor 13 of head tank: be used to measure storing lower limit situation in the feed hopper, give switching value signal of computer of electric cabinet, unite use with PLC.
11, head tank 14: being used for the splendid attire material, also is to launch blade 8, master screw with cyclone separator 4, connecting flange 5, spice bar 6, central rotating shaft 7, spiral to add the critical component that compressing tablet 9 etc. is united the work of feeding in raw material.The tapering of lower body will be good between 70 °~40 °.
12, the upper infrared inductor 15 of head tank: be used to measure storing upper limit case in the feed hopper 14, give switching value signal of computer of electric cabinet, so that stop associate device such as special-purpose pulverizer and conveying fan etc., can use the application that this switching signal that provides is write complete machine according to actual process.
When the utility model uses, the power-on switch, temperature is adjusted to setting value, temperature reaches the setting value back and opens the conveying fan starting button, the conveying fan back 2 minutes starting pulverizers that turn round, reinforced to pulverizer, wait the interior storing of head tank to last main motor, the reinforced buncher opened in limited time, the equipment input is normally used.

Claims (5)

1. the feeding mechanism of a comminutor, send into head tank (14) by the material that pulverizer (1) is pulverized through pipeline system, the material that enters head tank is delivered to main-machine screw (10) by rabbling mechanism, it is characterized in that: described rabbling mechanism is formed by stirring section and pressurized delivered section; Describedly stir the spice bar (6) that section is mounted in central rotating shaft (7) epimere, the spice bar (6) that described pressurized delivered section is mounted in central rotating shaft (7) hypomere and spiral launch blade (8) and the master screw of spice bar (6) below being positioned at spiral expansion blade and add compressing tablet (9) structure that matches.
2. the feeding mechanism of comminutor according to claim 1 is characterized in that: the spiral external diameter that described master screw adds compressing tablet (9) is 1: 1.2~1: 2 of main-machine screw (10) length; Pitch be master screw add compressing tablet (9) diameter 1/2~3/4, master screw adds compressing tablet (9) around the pitch of central rotating shaft (7) total length at 2~3 times.
3. the feeding mechanism of comminutor according to claim 1 and 2 is characterized in that: described master screw adds compressing tablet (9) and adopts double helix (91) around the spiral of central rotating shaft (7) about 1/4; The parameter of the helical blade that described double helix increased is identical with former helical blade, is connected former helical blade symmetric position in the same way.
4. the feeding mechanism of comminutor according to claim 1 and 2 is characterized in that: described spice bar (6) by spiral launch blade (8) direction become 120 ° spaced apart around central rotating shaft (7).
5. the feeding mechanism of comminutor according to claim 3 is characterized in that: described spice bar (6) by spiral launch blade (8) direction become 120 ° spaced apart around central rotating shaft (7).
CNU2007201060005U 2007-01-29 2007-01-29 Feeding mechanism of pelletizer Expired - Fee Related CN200998656Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2007201060005U CN200998656Y (en) 2007-01-29 2007-01-29 Feeding mechanism of pelletizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2007201060005U CN200998656Y (en) 2007-01-29 2007-01-29 Feeding mechanism of pelletizer

Publications (1)

Publication Number Publication Date
CN200998656Y true CN200998656Y (en) 2008-01-02

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Application Number Title Priority Date Filing Date
CNU2007201060005U Expired - Fee Related CN200998656Y (en) 2007-01-29 2007-01-29 Feeding mechanism of pelletizer

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102452159A (en) * 2010-10-22 2012-05-16 张家港市贝尔机械有限公司 Forced feeding device
CN109774008A (en) * 2019-03-11 2019-05-21 曹强 A kind of vertical plastic appearance machine
CN110027130A (en) * 2019-03-11 2019-07-19 曹强 A kind of working method of vertical plastic appearance machine
CN111495271A (en) * 2020-06-18 2020-08-07 广东睿智环保科技有限责任公司 Powder coating extruder

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102452159A (en) * 2010-10-22 2012-05-16 张家港市贝尔机械有限公司 Forced feeding device
CN109774008A (en) * 2019-03-11 2019-05-21 曹强 A kind of vertical plastic appearance machine
CN110027130A (en) * 2019-03-11 2019-07-19 曹强 A kind of working method of vertical plastic appearance machine
CN111495271A (en) * 2020-06-18 2020-08-07 广东睿智环保科技有限责任公司 Powder coating extruder

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20080102

Termination date: 20140129