CN204914284U - A DOP, DINP combination batching conveying system for PVC floor production line - Google Patents

A DOP, DINP combination batching conveying system for PVC floor production line Download PDF

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Publication number
CN204914284U
CN204914284U CN201520528626.XU CN201520528626U CN204914284U CN 204914284 U CN204914284 U CN 204914284U CN 201520528626 U CN201520528626 U CN 201520528626U CN 204914284 U CN204914284 U CN 204914284U
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CN
China
Prior art keywords
feed bin
dinp
dop
liquid material
material bucket
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
CN201520528626.XU
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Chinese (zh)
Inventor
郦海星
陈景
刘伟伟
张军华
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.)
Jiangsu Ruisheng New Materials Co Ltd
Original Assignee
Jiangsu Ruisheng New Materials 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
Publication date
Application filed by Jiangsu Ruisheng New Materials Co Ltd filed Critical Jiangsu Ruisheng New Materials Co Ltd
Priority to CN201520528626.XU priority Critical patent/CN204914284U/en
Application granted granted Critical
Publication of CN204914284U publication Critical patent/CN204914284U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a DOP, DINP combination batching conveying system for PVC floor production line, include that the DOP feed bin of vertical setting and the feed inlet of DINP feed bin and DOP feed bin and DINP feed bin all lie in its top, the bottom discharge gate of DOP feed bin loops through first petroleum pump and the first liquid hopper of pipeline connection, and the location discharge gate of DINP feed bin loops through second petroleum pump and the 2nd pipeline connection second liquid hopper, blanking mouth first, second liquid hopper is provided with the liquid electronic scale in connecting top feed inlet and the third liquid hopper of third liquid hopper jointly, and PVC floor production line compounding banburying system is connected to the bottom blanking mouth of third liquid hopper, the utility model discloses can be accurate quick control, supply and the mixture of carrying out DOP, DINP raw materials has improved work efficiency greatly, has reduced the waste of raw materials, has effectively reduced manufacturing cost.

Description

A kind of DOP, DINP combined ingredient induction system for PVC floor production line
Technical field
The utility model relates to the production and processing technical field of PVC floor, and spy is standby is a kind of DOP, DINP combined ingredient induction system for PVC floor production line.
Background technology
PVC floor is popular a kind of Novel light body floor decorative material in the world today, also referred to as " light body ground material "; A kind of product very popular in Japan and Korea S that are American-European and Asia, abroad fashionable, Chinese market is entered from the beginning of the eighties, so far big and medium-sized cities at home have obtained general accreditation, use widely, the various places such as such as family, hospital, school, office building, factory, public place, supermarket, business, stadiums; " PVC floor " just refers to the floor adopting pvc material to produce.Concrete be exactly with polyvinyl chloride and copolymer resins thereof for primary raw material, add the auxiliary materials such as filler, plasticizer, stabilizing agent, colouring agent, on sheet continuous base material, coated technique or through rolling, extruding or extrusion process produces.
Adopt coating process in existing PVC floor production line, rubbing method technique is numerous in variety more, and pattern variability is large, and productivity ratio is high, and output is large, and product specification is higher, but need use PVC paste resin; Generally, the polyvinyl chloride plastisol material prepared is coated on base material by apparatus for coating by rubbing method technological requirement, through pregel and cooling press polish, base material is just enclosed the certain thickness Corvic of one deck; Polyvinyl chloride plastisol is, by formula, PVC paste resin is scattered in the homogeneous colloidal dispersion formed in plasticizer by forceful action.
The existing large portion of paste resin yield for the production of artificial leather etc., every annual consumption about more than 20,000 ton, wherein more than 10,000 ton of dependence on import, therefore domestic PVC paste resin is natively very nervous, cannot meet the demand of plastic floor introduction of production line to paste resin; Therefore the raw material supply problem of PVC paste resin is put in face of us very shrilly; And domestic paste resin belongs to universal resin substantially, stick with paste viscosity and belong to medium, the needs of multi items user can not be adapted to; Except paste resin, the supply also difficulties of plasticizer, due to butanols and octanol lack of material, plasticizer is more nervous.
Utility model content
Technical problem to be solved in the utility model is, overcome the shortcoming of prior art, a kind of DOP, DINP combined ingredient induction system for PVC floor production line and application thereof are provided, the control of DOP, DINP raw material, supply and mixing can be carried out quickly and accurately, substantially increase operating efficiency, decrease the waste of raw material, effectively reduce production cost.
In order to solve above technical problem, the utility model provides a kind of DOP, DINP combined ingredient induction system for PVC floor production line, comprise the DOP feed bin and DINP feed bin that vertically arrange and the charging aperture of DOP feed bin and DINP feed bin is all positioned at its top, the bottom discharging opening of DOP feed bin connects the first liquid material bucket by the first oil transfer pump and the first conveyance conduit successively, and the location discharging opening of DINP feed bin connects the second liquid material bucket by the second oil transfer pump and the second conveyance conduit successively;
The blanking port of first, second liquid material bucket jointly connects the top charging aperture of the 3rd liquid material bucket and is provided with liquid electronic scale in the 3rd liquid material bucket, and the bottom blanking port of the 3rd liquid material bucket connects PVC floor production line batch mixing banburying system.
Technique effect: the conveying capacity of DOP, DINP combined ingredient induction system for PVC floor production line designed by the utility model can mate calcium carbonate and the PVC material induction system of 4-6T conveying capacity per hour, can adapt to the supply requirement of ultra-large floor production line;
Simultaneously, in the utility model, mass transport is that individual branc circuit carries mixing of integrating again, by the setting of the equipment such as first, second, third liquid material bucket, ensure that the cleaning of links feedstock transportation, precisely, during practical operation, PLC or long-range industry control section can be adopted effectively can either to control complete equipment, greatly save human cost, improve the efficiency of production, decrease the waste of raw material, effectively reduce production cost.
The technical scheme that the utility model limits further is:
Further, aforesaid DOP, DINP combined ingredient induction system for PVC floor production line, an operated pneumatic valve is respectively equipped with between the bottom discharging opening of DOP feed bin, DINP feed bin and first, second oil transfer pump, an operated pneumatic valve is respectively equipped with between first, second conveyance conduit and first, second liquid material bucket, be respectively equipped with an operated pneumatic valve between the blanking port of first, second liquid material bucket and the 3rd liquid material bucket, between the bottom blanking port of the 3rd liquid material bucket and PVC floor production line batch mixing banburying system, be provided with an operated pneumatic valve;
The upper and lower part sidewall of DOP feed bin and DINP feed bin is equipped with liquid level gauge, the upper and lower part sidewall of first and second liquid material bucket is equipped with liquid level gauge.
Aforesaid DOP, DINP combined ingredient induction system for PVC floor production line, the specification of DOP feed bin and DINP feed bin is 50m3, first, second oil transportation pump size is 5.5KW, and the specification of first, second liquid material bucket is 50L, and the specification of the 3rd liquid material bucket is 30L.
Accompanying drawing explanation
The structure principle chart of DOP, DINP combined ingredient induction system for PVC floor production line of Fig. 1 designed by the utility model.
Detailed description of the invention
Structure as shown in Figure 1, a kind of DOP, DINP combined ingredient induction system for PVC floor production line that the present embodiment provides, comprise the DOP feed bin and DINP feed bin that vertically arrange and the charging aperture of DOP feed bin and DINP feed bin is all positioned at its top, the bottom discharging opening of DOP feed bin connects the first liquid material bucket by the first oil transfer pump and the first conveyance conduit successively, and the location discharging opening of DINP feed bin connects the second liquid material bucket by the second oil transfer pump and the second conveyance conduit successively;
The blanking port of first, second liquid material bucket jointly connects the top charging aperture of the 3rd liquid material bucket and is provided with liquid electronic scale in the 3rd liquid material bucket, and the bottom blanking port of the 3rd liquid material bucket connects PVC floor production line batch mixing banburying system;
An operated pneumatic valve is respectively equipped with between the bottom discharging opening of DOP feed bin, DINP feed bin and first, second oil transfer pump, an operated pneumatic valve is respectively equipped with between first, second conveyance conduit and first, second liquid material bucket, be respectively equipped with an operated pneumatic valve between the blanking port of first, second liquid material bucket and the 3rd liquid material bucket, between the bottom blanking port of the 3rd liquid material bucket and PVC floor production line batch mixing banburying system, be provided with an operated pneumatic valve;
The upper and lower part sidewall of DOP feed bin and DINP feed bin is equipped with liquid level gauge, the upper and lower part sidewall of first and second liquid material bucket is equipped with liquid level gauge;
In actual production, we select the specification of DOP feed bin and DINP feed bin to be 50m3 according to actual needs, and first, second oil transportation pump size is 5.5KW, and the specification of first, second liquid material bucket is 50L, and the specification of the 3rd liquid material bucket is 30L.
The specific works principle of the present embodiment is: first, and liquid material, under the effect of first, second oil transfer pump of bottom, is delivered to first, second liquid material bucket respectively by first, second conveyance conduit by DOP feed bin and DINP feed bin;
In first, second liquid material bucket, liquid material enters the 3rd liquid material bucket jointly, and enters PVC floor production line batch mixing banburying system after liquid electronic scale weighs.
Above embodiment is only and technological thought of the present utility model is described; protection domain of the present utility model can not be limited with this; every technological thought according to the utility model proposes, any change that technical scheme basis is done, all falls within the utility model protection domain.

Claims (3)

1. DOP, DINP combined ingredient induction system for PVC floor production line, it is characterized in that, comprise the DOP feed bin and DINP feed bin that vertically arrange and the charging aperture of described DOP feed bin and DINP feed bin is all positioned at its top, the bottom discharging opening of described DOP feed bin connects the first liquid material bucket by the first oil transfer pump and the first conveyance conduit successively, and the location discharging opening of described DINP feed bin connects the second liquid material bucket by the second oil transfer pump and the second conveyance conduit successively;
The blanking port of first, second liquid material bucket described jointly connects the top charging aperture of the 3rd liquid material bucket and is provided with liquid electronic scale in described 3rd liquid material bucket, and the bottom blanking port of described 3rd liquid material bucket connects PVC floor production line batch mixing banburying system.
2. the DOP for PVC floor production line according to claim 1, DINP combined ingredient induction system, it is characterized in that, described DOP feed bin, the bottom discharging opening of DINP feed bin and first, an operated pneumatic valve is respectively equipped with between second oil transfer pump, described first, second conveyance conduit and first, an operated pneumatic valve is respectively equipped with between second liquid material bucket, described first, an operated pneumatic valve is respectively equipped with between the blanking port of the second liquid material bucket and the 3rd liquid material bucket, an operated pneumatic valve is provided with between the bottom blanking port of described 3rd liquid material bucket and PVC floor production line batch mixing banburying system,
The upper and lower part sidewall of described DOP feed bin and DINP feed bin is equipped with liquid level gauge, the upper and lower part sidewall of first and second liquid material bucket described is equipped with liquid level gauge.
3. DOP, DINP combined ingredient induction system for PVC floor production line according to claim 1 and 2, it is characterized in that, the specification of described DOP feed bin and DINP feed bin is 50m3, first, second oil transportation pump size described is 5.5KW, the specification of first, second liquid material bucket described is 50L, and the specification of described 3rd liquid material bucket is 30L.
CN201520528626.XU 2015-07-20 2015-07-20 A DOP, DINP combination batching conveying system for PVC floor production line Expired - Fee Related CN204914284U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520528626.XU CN204914284U (en) 2015-07-20 2015-07-20 A DOP, DINP combination batching conveying system for PVC floor production line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520528626.XU CN204914284U (en) 2015-07-20 2015-07-20 A DOP, DINP combination batching conveying system for PVC floor production line

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CN204914284U true CN204914284U (en) 2015-12-30

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105058610A (en) * 2015-07-20 2015-11-18 江苏锐升新材料有限公司 Dioctyl phthalate (DOP) and diisononyl phthalate (DINP) combined proportioning and conveying system for polyvinyl chloride (PVC) floor production line

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105058610A (en) * 2015-07-20 2015-11-18 江苏锐升新材料有限公司 Dioctyl phthalate (DOP) and diisononyl phthalate (DINP) combined proportioning and conveying system for polyvinyl chloride (PVC) floor production line

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

Granted publication date: 20151230

Termination date: 20180720