CN203887890U - Polystyrene melting device - Google Patents
Polystyrene melting device Download PDFInfo
- Publication number
- CN203887890U CN203887890U CN201420206251.0U CN201420206251U CN203887890U CN 203887890 U CN203887890 U CN 203887890U CN 201420206251 U CN201420206251 U CN 201420206251U CN 203887890 U CN203887890 U CN 203887890U
- Authority
- CN
- China
- Prior art keywords
- blanking tube
- material blanking
- pneumatic cylinder
- cutting
- polystyrene
- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
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- Crushing And Pulverization Processes (AREA)
Abstract
The utility model provides a polystyrene melting device. The device comprises a rubber cutting part, a blanking part and a melting part; the rubber cutting part comprises a rack, a pneumatic cylinder, a cutter, a cutting plate and a baffle plate; a fixing plate is rotatably connected to the top part of the rack; a pneumatic cylinder mounting hole in which the pneumatic cylinder is mounted is formed in the fixing plate; the output end of the pneumatic cylinder is connected with a cutter seat; a cutter is connected with the cutter seat; the cutting plate is fixed to the lower middle part of the rack; the baffle is rotatably connected to the bottom part of the rack; the blanking part consists of a vertical blanking pipe and a rotating blanking pipe; a circular annular groove is formed in the bottom part of the vertical blanking pipe; a circular annular platform that is clamped into the circular annular groove is fixed to the top end of the rotating blanking pipe; the melting part is a circulating ultramicro air-jet pulverizing fluidized bed boiler. The polystyrene melting device has the characteristics that the functions of rubber cutting, blanking and rubber smelting are integrated, so that the practicability is high; efficient and standard rubber cutting can be carried out, continuous production is realized, thus the production efficiency is improved, and the enterprise benefit is increased.
Description
Technical field
The invention belongs to polystyrene manufacturing and processing equipment field, be specifically related to a kind of polystyrene melting plant.
Background technology
First p-poly-phenyl ethene carries out melting needs polystyrene colloid to be carried in bale splitter, and glue to be cut enters after completing again and in glue pot, carries out melting.
For more current middle-size and small-size and ground zero type enterprises, need to rely on operator to carry out Manual material feeding; In order to protect the cutter in bale splitter, polystyrene colloid need to be dropped in bale splitter lentamente, add polystyrene colloid heavier, therefore both time-consuming also effort of current Manual material feeding.Polystyrene colloid starts to cut glue after entering bale splitter, cutter in existing bale splitter is mostly cut glue by High Rotation Speed, the high speed rotating of cutter can cause beating of the interior polystyrene colloid of bale splitter, not only extended and cut the glue time, reduce and cut glue efficiency, also can make the polystyrene colloidal block size having cut differ simultaneously, cause the melting time to control.
In order to enhance productivity to greatest extent, generally a larger polystyrene colloid can be put into bale splitter and carry out disposable gel cutting, therefore it is longer to cut the glue time, be approximately 3 hours, cutting glue enters after completing and in glue pot, carries out melting and need about 9 hours, even if complete and cut glue and once cut glue on carrying out after carrying out melting at once at bale splitter, also there is the free time of about 3 hours in bale splitter, and can not maximally utilise limited equipment is that enterprise produces income.
Therefore, develop and a kind ofly can carry out standard, efficiently cut glue, and can guarantee that quantity-produced polystyrene melting plant is the problem of the required solution of those skilled in the art.
Summary of the invention
In order to address the above problem, to the invention provides and a kind ofly can carry out standard, efficiently cut glue and the polystyrene melting plant that can uninterruptedly produce continuously.
In order to achieve the above object, the invention provides following technical scheme:
A polystyrene melting plant, comprises and cuts glue portion, blanking portion and fusing department; Cutting glue portion is comprised of frame, pneumatic cylinder, cutting knife, cutting plate and baffle plate; The top of frame is rotatably connected to fixed head, and fixed head is provided with pneumatic cylinder installing hole; Pneumatic cylinder is installed in pneumatic cylinder installing hole, and the output of pneumatic cylinder is connected with tool rest; Cutting knife is connected with tool rest; Cutting plate is fixed on the middle and lower part of frame; Baffle plate is rotationally connected with the bottom of frame; Blanking portion comprises vertical material blanking tube and rotation material blanking tube; Vertically the bottom of material blanking tube is provided with circle shape groove, and circle shape groove is divided into upper pipe and lower pipe by vertical material blanking tube; The top of rotation material blanking tube is fixed with circular platform; Circular platform card is in circle shape groove; Fusing department is circulation ultra micro air-flow crushing fluidized-bed combustion boiler, and the charging aperture of circulation ultra micro air-flow crushing fluidized-bed combustion boiler is connected with the bottom of rotation material blanking tube.
The present invention forms by cutting glue portion, blanking portion and fusing department, integrates and cuts glue, blanking and melten gel function.
Cutting glue portion is comprised of frame, pneumatic cylinder, cutting knife, cutting plate and baffle plate; The top of frame is rotatably connected to fixed head, and fixed head is provided with pneumatic cylinder installing hole; Pneumatic cylinder is installed in pneumatic cylinder installing hole, and the output of pneumatic cylinder is connected with tool rest; Cutting knife is connected with tool rest; Cutting plate is fixed on the middle and lower part of frame; Baffle plate is rotationally connected with the bottom of frame.Pneumatic cylinder is installed on fixed head, and is rotationally connected with frame top, in the time of need to feeding intake, rotate fixed head fixed head is opened, after having fed intake, again rotate fixed head cuts out; The output of pneumatic cylinder is connected with tool rest, and cutting knife is installed on tool rest, by pneumatic cylinder output, drives cutting knife to move back and forth, and p-poly-phenyl ethene colloid cuts, and after having cut, opens baffle plate, makes the polystyrene blob of viscose of well cutting enter blanking portion.
Blanking portion comprises vertical material blanking tube and rotation material blanking tube; Vertically the bottom of material blanking tube is provided with circle shape groove, and circle shape groove is divided into upper pipe and lower pipe by vertical material blanking tube; The top of rotation material blanking tube is fixed with circular platform; Circular platform card is in circle shape groove.Blanking portion is comprised of vertical material blanking tube and rotation material blanking tube; Vertically the bottom of material blanking tube is provided with circle shape groove, and the top of rotation material blanking tube is fixed with circular platform, by circular platform card in circle shape groove, to realize the rotating function of rotation material blanking tube.
Fusing department is used circulation ultra micro air-flow crushing fluidized-bed combustion boiler, the NO producing in the time of can reducing molten polystyrene
xdischarge, and improve desulfurization degree, accomplish clean burning; The strong adaptability of circulation ultra micro air-flow crushing fluidized-bed combustion boiler to fuel, efficiency of combustion is high; And load adaptability is good.
As preferably, the quantity of circulation ultra micro air-flow crushing fluidized-bed combustion boiler is three, and the charging aperture of three circulation ultra micro air-flow crushing fluidized-bed combustion boilers is all identical to the distance of rotating material blanking tube.
The present invention is designed to three by the quantity of circulation ultra micro air-flow crushing fluidized-bed combustion boiler, cuts common needs of glue time about 3 hours, and the melten gel time needs about 9 hours; After cutting glue for the first time, make polystyrene blob of viscose fall into first circulation ultra micro air-flow crushing fluidized-bed combustion boiler and carry out melting; Cut for the second time immediately glue, polystyrene blob of viscose is dropped in second circulation ultra micro air-flow crushing fluidized-bed combustion boiler and carries out melting; Finally cut for the third time glue, polystyrene blob of viscose is dropped into the 3rd circulation ultra micro air-flow crushing fluidized-bed combustion boiler and carry out melting; When cutting glue the 4th time and complete, primary polystyrene blob of viscose also in circulation ultra micro air-flow crushing fluidized-bed combustion boiler melting complete, discharge after polystyrene fluid and to complete to drop in first circulation ultra micro air-flow crushing fluidized-bed combustion boiler and carry out melting cutting glue for the 4th time, so repeatedly, realize continuously and producing.
The present invention also makes charging aperture to the distance of rotating material blanking tube of three circulation ultra micro air-flow crushing fluidized-bed combustion boilers be set to equate, making only to need to rotate rotation material blanking tube just can drop into the polystyrene blob of viscose of well cutting in circulation ultra micro air-flow crushing fluidized-bed combustion boiler, without the position of adjusting circulation ultra micro air-flow crushing fluidized-bed combustion boiler, time saving and energy saving.
As preferably, the madial wall of frame is provided with guide rail by top to middle and lower part, and the bottom of guide rail is provided with restriction platform; Tool rest is all fixed with the edge of cutting plate the slide block matching with guide rail; Limit on platform and be fixed with spring.
The present invention is cutting on the madial wall of glue portion frame, by fixed head place, top to middle and lower part cutting plate, goes out to be provided with guide rail, and is all fixed with the edge of cutting plate the slide block matching with guide rail at tool rest; Guide rail and slide block form guider jointly, make cutting knife more stable when p-poly-phenyl ethene colloid cuts; And in the bottom of guide rail, be provided with restriction platform, on restriction platform, be fixed with spring, cutting plate is placed on spring, make to leave buffering when cutting polystyrene colloid, cutting knife is played to certain protective role, extend the service life of cutting knife, reduce maintenance times.
As preferably, cutting knife is comprised of horizontal cutting knife group and longitudinal cutter group, and laterally cutting knife group is connected with longitudinal cutter group is vertical, forms latticed cutting knife; It is latticed that cutting plate is similarly, and its grid is greater than the grid of horizontal cutting knife group and longitudinal cutter group formation.
Cutting knife in the present invention is connected and composed with longitudinal cutter group is vertical by horizontal cutting knife group, forms latticed cutting knife; And cutting plate is also made as latticed, and the grid of cutting plate is greater than the grid that horizontal cutting knife group and longitudinal cutter group form, and cutting knife can be dropped on the polystyrene blob of viscose of polystyrene colloid cut growth strip on baffle plate by the network of cutting plate.
As preferably, to cut glue portion and also comprise feed belt and vacuum cup, the upper end of feed belt is connected with the top of frame; Vacuum cup is slidably mounted on feed belt to the top of frame by guide groove.
The glue portion of cutting of the present invention also has additional feed belt and vacuum cup, and feed belt is tilted to arrangement, and its upper end is connected with frame top edge; The top of feed belt and frame is also slidably fitted with vacuum cup by guide groove; Carrying out polystyrene colloid while feeding intake, polystyrene colloid is placed on to the lower end of feed belt, and be fixed by vacuum cup, transmission along with feed belt, with the polystyrene colloid of vacuum cup, arrive the upper end of feed belt, now only need vacuum slide sucker just polystyrene colloid can be sent in cutting part, alleviated operator's labour intensity.
As preferably, the diameter of upper pipe is greater than the diameter of lower pipe; The degree of depth of circle shape groove and circular platform equal in length, and bearing is also installed between circular platform and circle shape groove.
Vertically the upper pipe diameter of material blanking tube is greater than lower pipe diameter, and the degree of depth of circle shape groove and circular platform is equal in length, and circular platform just in time can be sticked in circle shape groove, has strengthened the stability of blanking portion; The present invention is also also provided with bearing between circular platform and circle shape groove, the friction in the time of can reducing the rotation of rotation material blanking tube.
As preferably, the bottom margin of upper pipe is evenly distributed with four La Erka; The top of rotation material blanking tube is provided with a circle groove, and groove matches with La Erka.
Upper Guan Yusi La Erka forms female joint, and the rotation material blanking tube that top has a circle groove forms male joint, jointly forms Earrings type snap joint, utilizes eccentric center principle that the groove of male joint can just be blocked by the La Erka of female joint, realizes self-locking; Make vertical material blanking tube and rotation material blanking tube not need use instrument just can interfix.
The present invention compares with existing polystyrene melting plant, set up feed belt and the vacuum cup that can solve polystyrene colloid carrying problem, the latticed cutting knife that can p-poly-phenyl ethene colloid carries out standard cutting, and the rotation material blanking tube that is provided with three circulation ultra micro air-flow crushing fluidized-bed combustion boilers and can rotates, therefore beneficial effect of the present invention is: (1) integrates and cuts glue, blanking and melten gel function, practical; (2) can carry out efficient, standard and cut glue; (3) can realize continuous production, enhance productivity, improve enterprise income.
Accompanying drawing explanation
Fig. 1, structural representation of the present invention;
Vertical material blanking tube and the schematic diagram that rotates material blanking tube junction in Fig. 2, the present invention.
Reference numerals list: frame 1, pneumatic cylinder 2, cutting knife 3, cutting plate 4, baffle plate 5, fixed head 6, tool rest 7, vertically material blanking tube 8, rotation material blanking tube 9, circulation ultra micro air-flow crushing fluidized-bed combustion boiler 10, guide rail 11, limit platform 12, slide block 13, feed belt 14, vacuum cup 15, guide groove 16, bearing 17, draw ear card 18, groove 19.
The specific embodiment
Below with reference to specific embodiment, technical scheme provided by the invention is elaborated, should understands the following specific embodiment and only for the present invention is described, is not used in and limits the scope of the invention.
Be illustrated in figure 1 structural representation of the present invention.
The present invention is a kind of polystyrene melting plant, comprises and cuts glue portion, blanking portion and fusing department.
Cutting glue portion is comprised of frame 1, pneumatic cylinder 2, cutting knife 3, cutting plate 4 and baffle plate 5; The top of frame 1 is rotatably connected to fixed head 6, and fixed head 6 is provided with pneumatic cylinder installing hole; Pneumatic cylinder 2 is installed in pneumatic cylinder installing hole, and the output of pneumatic cylinder 2 is connected with tool rest 7; Cutting knife 3 is connected with tool rest 7; Cutting knife 3 is comprised of horizontal cutting knife group and longitudinal cutter group, and laterally cutting knife group is connected with longitudinal cutter group is vertical, forms latticed cutting knife; Cutting plate 4 is fixed on the middle and lower part of frame 1; Cutting plate 4 is similarly latticed, and its grid is greater than the grid of horizontal cutting knife group and longitudinal cutter group formation; Baffle plate 5 is rotationally connected with the bottom of frame 1; The madial wall of frame 1 is provided with guide rail 11 by top to middle and lower part, and the bottom of guide rail 11 is provided with and limits platform 12; Tool rest 7 is all fixed with the edge of cutting plate 4 slide block 13 matching with guide rail 11; Limit on platform 12 and be fixed with spring; The top of frame 1 is also connected with feed belt 14; Feed belt 14 to the top of frame 1 is provided with guide groove 16, is slidably fitted with vacuum cup 15 on guide groove 16.
Blanking portion comprises vertical material blanking tube 8 and rotation material blanking tube 9; As shown in Figure 2, Fig. 2 is vertical material blanking tube and the schematic diagram that rotates material blanking tube junction in the present invention; Vertically the bottom of material blanking tube 8 is provided with circle shape groove, and circle shape groove is divided into upper pipe and lower pipe by vertical material blanking tube 8; The diameter of upper pipe is greater than the diameter of lower pipe; The bottom margin of upper pipe is evenly distributed with four and draws ear card 18; The top of rotation material blanking tube 9 is provided with a circle groove 19, and groove 19 matches with drawing ear card 18; The top of rotation material blanking tube is fixed with circular platform; The degree of depth of circle shape groove and circular platform equal in length; Circular platform card is in circle shape groove; Bearing 17 is also installed between circular platform and circle shape groove.
Fusing department is circulation ultra micro air-flow crushing fluidized-bed combustion boiler 10, and the charging aperture of circulation ultra micro air-flow crushing fluidized-bed combustion boiler 10 is connected with the bottom of rotation material blanking tube 9; The quantity of circulation ultra micro air-flow crushing fluidized-bed combustion boiler 10 is three, and the charging aperture of three circulation ultra micro air-flow crushing fluidized-bed combustion boilers 10 is all identical to the distance of rotating material blanking tube 9.
With specific embodiment, illustrate below:
Larger polystyrene colloid is used vacuum cup 15 fixing, along with feed belt 14 is sent to frame 1 top, opens fixed head 6, by Mobile vacuum sucker 15, polystyrene is fallen on the cutting plate 4 of frame 1, closes fixed head 6; Start pneumatic cylinder 2, under the impetus of pneumatic cylinder 2, the tool rest 7 being connected with pneumatic cylinder 2 outputs drives the polystyrene colloid on 3 pairs of cutting plates 4 of cutting knife to cut, latticed cutting knife 3 cuts into polystyrene colloid the polystyrene blob of viscose of strip, the polystyrene blob of viscose having cut drops on baffle plate 5, open afterwards baffle plate 5, polystyrene blob of viscose is entered in first circulation ultra micro air-flow crushing fluidized-bed combustion boiler 10 and carries out melten gel with rotation material blanking tube 9 by vertical material blanking tube 8, and this process completes about needs 3 hours.
Afterwards, open and draw ear card 18 on vertical material blanking tube 8, rotate rotation material blanking tube 9, it is connected with second circulation ultra micro air-flow crushing fluidized-bed combustion boiler 10, then repeats above step and carry out melten gel for the second time, then need 3 hours.
Subsequently, repeat above step and carry out melten gel for the third time, need 3 hours; Now melten gel completes for the first time, discharges the polystyrene fluid in first circulation ultra micro air-flow crushing fluidized-bed combustion boiler 10, then carries out the 4th time and cut glue and melten gel.
Repeat above step and just can realize continuous production.
The disclosed technological means of the present invention program is not limited only to the disclosed technological means of above-mentioned embodiment, also comprises the technical scheme being comprised of above technical characterictic.
Claims (7)
1. a polystyrene melting plant, is characterized in that: comprise and cut glue portion, blanking portion and fusing department; The described glue portion of cutting is comprised of frame (1), pneumatic cylinder (2), cutting knife (3), cutting plate (4) and baffle plate (5); The top of described frame (1) is rotatably connected to fixed head (6), and fixed head (6) is provided with pneumatic cylinder installing hole; Described pneumatic cylinder (2) is installed in pneumatic cylinder installing hole, and the output of pneumatic cylinder (2) is connected with tool rest (7); Described cutting knife (3) be connected with tool rest (7); Described cutting plate (4) is fixed on the middle and lower part of frame (1); Described baffle plate (5) is rotationally connected with the bottom of frame (1); Described blanking portion comprises vertical material blanking tube (8) and rotation material blanking tube (9); The bottom of described vertical material blanking tube (8) is provided with circle shape groove, and circle shape groove is divided into upper pipe and lower pipe by vertical material blanking tube (8); The top of described rotation material blanking tube (9) is fixed with circular platform; Described circular platform card is in circle shape groove; Described fusing department is circulation ultra micro air-flow crushing fluidized-bed combustion boiler (10), and the charging aperture of circulation ultra micro air-flow crushing fluidized-bed combustion boiler (10) is connected with the bottom of rotation material blanking tube (9).
2. a kind of polystyrene melting plant according to claim 1, it is characterized in that: the quantity of described circulation ultra micro air-flow crushing fluidized-bed combustion boiler (10) is three, and the charging aperture of three circulation ultra micro air-flow crushing fluidized-bed combustion boilers (10) is all identical to the distance of rotating material blanking tube (9).
3. a kind of polystyrene melting plant according to claim 1, is characterized in that: the madial wall of described frame (1) is provided with guide rail (11) by top to middle and lower part, and the bottom of guide rail (11) is provided with and limits platform (12); Described tool rest (7) is all fixed with the edge of cutting plate (4) slide block (13) matching with guide rail (11); On described restriction platform (12), be fixed with spring (13).
4. a kind of polystyrene melting plant according to claim 1, is characterized in that: described cutting knife (3) is comprised of horizontal cutting knife group and longitudinal cutter group, and laterally cutting knife group is connected with longitudinal cutter group is vertical, forms latticed cutting knife; Described cutting plate (4) is similarly latticed, and its grid is greater than the grid of horizontal cutting knife group and longitudinal cutter group formation.
5. a kind of polystyrene melting plant according to claim 1, is characterized in that: described in cut glue portion and also comprise feed belt (14) and vacuum cup (15), the upper end of feed belt (14) is connected with the top of frame (1); Described vacuum cup (15) is slidably mounted on feed belt (14) to the top of frame (1) by guide groove (16).
6. a kind of polystyrene melting plant according to claim 1, is characterized in that: the diameter of described upper pipe is greater than the diameter of lower pipe; The degree of depth of described circle shape groove and circular platform equal in length, and bearing (17) is also installed between circular platform and circle shape groove.
7. a kind of polystyrene melting plant according to claim 1, is characterized in that: the bottom margin of described upper pipe is evenly distributed with four La Erka (18); The top of described rotation material blanking tube (9) is provided with a circle groove (19), and groove (19) matches with La Erka (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420206251.0U CN203887890U (en) | 2014-04-25 | 2014-04-25 | Polystyrene melting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420206251.0U CN203887890U (en) | 2014-04-25 | 2014-04-25 | Polystyrene melting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203887890U true CN203887890U (en) | 2014-10-22 |
Family
ID=51714336
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420206251.0U Expired - Fee Related CN203887890U (en) | 2014-04-25 | 2014-04-25 | Polystyrene melting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203887890U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103963086A (en) * | 2014-04-25 | 2014-08-06 | 江苏赛宝龙石化有限公司 | Polystyrene fusion device |
-
2014
- 2014-04-25 CN CN201420206251.0U patent/CN203887890U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103963086A (en) * | 2014-04-25 | 2014-08-06 | 江苏赛宝龙石化有限公司 | Polystyrene fusion device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141022 Termination date: 20160425 |