CN211842820U - Polymer toughening spray-melting geomembrane processing device - Google Patents

Polymer toughening spray-melting geomembrane processing device Download PDF

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Publication number
CN211842820U
CN211842820U CN201922447229.0U CN201922447229U CN211842820U CN 211842820 U CN211842820 U CN 211842820U CN 201922447229 U CN201922447229 U CN 201922447229U CN 211842820 U CN211842820 U CN 211842820U
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CN
China
Prior art keywords
cooler
pipe
hot air
melting
rough
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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.)
Expired - Fee Related
Application number
CN201922447229.0U
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Chinese (zh)
Inventor
宋涛
乔秀海
郑庆超
马智辉
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Shandong Lingxiang New Material Co Ltd
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Shandong Lingxiang New Material Co Ltd
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Priority to CN201922447229.0U priority Critical patent/CN211842820U/en
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Publication of CN211842820U publication Critical patent/CN211842820U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model relates to a polymer is toughened and is spouted and melt geomembrane processingequipment, including spouting rough device, it is provided with the heating cabinet to spout rough device front end, be provided with two warming mill in the heating cabinet, it is provided with the cooler bin to spout rough device rear end, the cooler bin rear end is provided with material collecting device, it includes the hot-blast main of being connected with hot-blast source and the fuse-element passageway of being connected with the melt device to spout rough device, the hot-blast main is connected to the hot-blast main, a set of hot-blast branch pipe is connected to the guide duct, melt channel connects plate die head, be provided with a set of discharge nozzle on the plate die head, discharge nozzle with hot-blast branch pipe quantity is unanimous, just discharge nozzle is connected with the hot-blast branch pipe that corresponds.

Description

Polymer toughening spray-melting geomembrane processing device
Technical Field
The utility model belongs to the technical field of the geomembrane technique and specifically relates to a polymer is toughened and is spouted and melt geomembrane processingequipment.
Background
The geomembrane is a geotechnical anti-seepage material which is compounded by a plastic film serving as an anti-seepage base material and non-woven fabrics, and the anti-seepage performance of the geomembrane mainly depends on the anti-seepage performance of the plastic film. The blow molding machine is used for blowing the plastic body to a mold cavity with a certain shape by utilizing the wind power blown out by the machine after the liquid plastic is sprayed out, thereby manufacturing the product.
In the prior art, the geomembrane blow molding machine has the technical problem that the productivity, materials and quality cannot reach the standard in the roughening process for producing the geomembrane, so that corresponding treatment and modification are carried out, and different roughening processes for producing the geomembrane have different technical problems.
SUMMERY OF THE UTILITY MODEL
To the technical problem, the utility model provides a geomembrane equipment of roughening has solved the not up to standard technical problem of coefficient of friction that geomembrane blowing machine appears at production geomembrane in-process.
The utility model provides a technical scheme that its technical problem adopted is:
a macromolecule toughening spraying and melting geomembrane processing device comprises a spraying device, wherein a heating box is arranged at the front end of the spraying device, two heating rollers are arranged in the heating box, a cooling box is arranged at the rear end of the spraying device, a material receiving device is arranged at the rear end of the cooling box, the spraying device comprises a hot air pipe connected with a hot air source and a melt channel connected with a melt device, the hot air pipe is connected with an air guide pipe, the air guide pipe is connected with a group of hot air branch pipes, the melt channel is connected with a plate type die head, a group of discharging nozzles are arranged on the plate type die head, the number of the discharging nozzles is consistent with that of the hot air branch pipes, and the discharging nozzles are connected with the corresponding hot air branch pipes;
the cooling box comprises a cold water circulator, the cold water circulator is arranged in the cooling box and is connected with a water delivery pipe and a water return pipe, the water delivery pipe is connected with a first cooler, the water return pipe is connected with a second cooler, the first cooler and the second cooler are connected through a communicating pipe, the first cooler and the second cooler are arranged on a transparent baffle, the transparent baffle is arranged above the base film, and a fan is arranged at the top of the cooling box.
Further optimally, a voltage stabilizer is arranged on the hot air branch pipe.
Further optimally, the material receiving device comprises a guide roller and a material receiving roller.
Further optimally, a heat preservation channel is arranged between the heating box and the rough spraying device.
Further optimally, an insulating layer is arranged in the heating box.
The utility model has the advantages that:
the heating box is internally provided with two heating rollers, the base film passes through the two heating rollers to preheat the base film, and the heating box is internally provided with a heat preservation layer to prevent heat loss and save energy;
the pressure stabilizer is arranged on the hot air branch pipe, so that the pressure of each discharging nozzle is consistent, and the material spraying is more uniform;
the cooling box that sets up makes the base film after spouting rough cool off fast, and the later stage of being convenient for is received the material.
The utility model relates to a rationally, make and spout coarse effect more even, avoided the not up to standard technical problem of coefficient of friction
Drawings
The present invention will be further explained with reference to the drawings and examples.
Fig. 1 is a schematic structural diagram of the present invention;
in the figure, 1, a heating box, 2, a heating roller, 3, a heat preservation channel, 4, a rough spraying device, 5, a plate type die head, 6, a discharging nozzle, 7, a hot air branch pipe, 8, a voltage stabilizer, 9, an air guide pipe, 10, a hot air pipe, 11, a solution channel, 12, a cooling box, 13, a water conveying pipe, 14, a cold water circulator, 15, a water return pipe, 16, a first cooler, 17, a communicating pipe, 18, a second cooler, 19, a fan, 20, a transparent baffle, 21, a base film, 22, a guide roller and 23, a material collecting roller are arranged.
Detailed Description
The preferred embodiments of the present invention will be described in conjunction with the accompanying drawings, and it will be understood that they are presented herein only to illustrate and explain the present invention, and not to limit the present invention.
Wherein like reference numerals refer to like parts throughout.
In addition, if a detailed description of the known art is not necessary to show the features of the present invention, it is omitted. It should be noted that the terms "front," "back," "left," "right," "upper" and "lower" used in the following description refer to directions in the drawings, and the terms "inner" and "outer" refer to directions toward and away from, respectively, the geometric center of a particular component.
It should also be noted that, unless expressly stated or limited otherwise, the terms "disposed" and "connected" are to be construed broadly, e.g., as meaning fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. To those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood in specific instances, and furthermore, the terms "first", "second", and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
As shown in figure 1, a macromolecule toughening spraying and melting geomembrane processing device comprises a spraying device 4, wherein a heating box 1 is arranged at the front end of the spraying device 4, two heating rollers 2 are arranged in the heating box 1, a base film 21 passes through the two heating rollers 2 to preheat the base film, a heat insulating layer is arranged in the heating box 1 to prevent heat loss and save energy, a heat insulating channel 3 is arranged between the heating box 1 and the spraying device 4 in the heating box, a cooling box 12 is arranged at the rear end of the spraying device 4 to rapidly cool and fix the base film after being sprayed with roughness through the arranged cooling box so as to facilitate subsequent material collection, a material collecting device is arranged at the rear end of the cooling box 12 and comprises a guide roller 22 and a material collecting roller 23, the material collecting device is used for changing the reverse direction of the base film 21 by arranging the guide roller 22 so as to facilitate the material collection of the material collecting roller 23, the spraying device 4 comprises a hot air pipe 10 connected with a hot air source and a melt channel 11 connected with the melting device, the hot air pipe 10 is connected with an air guide pipe 9, the air guide pipe 9 is connected with a group of hot air branch pipes 7, a voltage stabilizer 8 is arranged on each hot air branch pipe 7, the melt channel 11 is connected with the plate type die head 5, a group of discharging nozzles 6 are arranged on the plate type die head 5, the number of the discharging nozzles 6 is the same as that of the hot air branch pipes 7, the discharging nozzles 6 are connected with the corresponding hot air branch pipes 7, the hot melt granules are sprayed and diffused to the surface of the base film under the action of hot air, and the hot air plays roles in maintaining the temperature of the melt granules, scattering the melt granules and preheating the film material; the arranged voltage stabilizer 8 packs all the discharge nozzles to have consistent pressure, so that the sprayed material is uniform;
in order to rapidly cool the rough sprayed base film, a cooling tank 12 is arranged at the rear side of the rough spraying device 4, the cooling tank 12 comprises a cold water circulator 14, the cooling tank 12 is internally provided with the cold water circulator 14, the cold water circulator 14 is connected with a water conveying pipe 13 and a water return pipe 15, the water conveying pipe 14 is connected with a first cooler 16, the water return pipe 15 is connected with a second cooler 18, the first cooler 16 and the second cooler 18 are connected through a communication pipe 17, the first cooler 16 and the second cooler 18 are arranged on a transparent baffle 20, the transparent baffle 20 is arranged above the base film 21, and a fan 19 is arranged at the top of the cooling tank 12.
The first cooler 16 and the second cooler 18 are started, the two coolers work, cold water enters the first cooler 16 and the second cooler 18 through the water conveying pipe 13, the cold water flowing fast keeps the communicating pipe 17 in a cold state all the time, normal-temperature wind generated by the fan is fast cooled into cold wind, the cold wind flows back to the cooling water circulator 14 through the water return pipe 15, and when products pass through the lower portions of the first cooler 16 and the second cooler 18, the cold wind enables the products to be fast cooled, so that the effect of cooling the products is achieved.
In light of the foregoing, it will be apparent to those skilled in the art from this disclosure that various changes and modifications can be made without departing from the spirit and scope of the invention. The technical scope of the present invention is not limited to the content of the specification, and must be determined according to the scope of the claims.

Claims (5)

1. The utility model provides a polymer is toughened and is spouted and melt geomembrane processingequipment, is including spouting rough device, it is provided with the heating cabinet to spout rough device front end, be provided with two warming mill in the heating cabinet, it is provided with the cooler bin to spout rough device rear end, the cooler bin rear end is provided with material collecting device, its characterized in that: the rough spraying device comprises a hot air pipe connected with a hot air source and a melt channel connected with a melt melting device, the hot air pipe is connected with an air guide pipe, the air guide pipe is connected with a group of hot air branch pipes, the melt channel is connected with a plate type die head, a group of discharging nozzles are arranged on the plate type die head, the number of the discharging nozzles is consistent with that of the hot air branch pipes, and the discharging nozzles are connected with the corresponding hot air branch pipes;
the cooling box comprises a cold water circulator, the cold water circulator is arranged in the cooling box and is connected with a water delivery pipe and a water return pipe, the water delivery pipe is connected with a first cooler, the water return pipe is connected with a second cooler, the first cooler and the second cooler are connected through a communicating pipe, the first cooler and the second cooler are arranged on a transparent baffle, the transparent baffle is arranged above the base film, and a fan is arranged at the top of the cooling box.
2. The processing device of the high polymer toughening spray-melting geomembrane according to claim 1, characterized in that: the hot air branch pipe is provided with a voltage stabilizer.
3. The processing device of the high polymer toughening spray-melting geomembrane according to claim 1, characterized in that: the material receiving device comprises a guide roller and a material receiving roller.
4. The processing device of the high polymer toughening spray-melting geomembrane according to claim 1, characterized in that: and a heat insulation channel is arranged between the heating box and the rough spraying device.
5. The processing device of the high polymer toughening spray-melting geomembrane according to claim 1, characterized in that: and a heat insulation layer is arranged in the heating box.
CN201922447229.0U 2019-12-27 2019-12-27 Polymer toughening spray-melting geomembrane processing device Expired - Fee Related CN211842820U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201922447229.0U CN211842820U (en) 2019-12-27 2019-12-27 Polymer toughening spray-melting geomembrane processing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201922447229.0U CN211842820U (en) 2019-12-27 2019-12-27 Polymer toughening spray-melting geomembrane processing device

Publications (1)

Publication Number Publication Date
CN211842820U true CN211842820U (en) 2020-11-03

Family

ID=73209334

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201922447229.0U Expired - Fee Related CN211842820U (en) 2019-12-27 2019-12-27 Polymer toughening spray-melting geomembrane processing device

Country Status (1)

Country Link
CN (1) CN211842820U (en)

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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20201103

CF01 Termination of patent right due to non-payment of annual fee