CN205097392U - Silica gel mill base continuous production system - Google Patents

Silica gel mill base continuous production system Download PDF

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Publication number
CN205097392U
CN205097392U CN201520784767.8U CN201520784767U CN205097392U CN 205097392 U CN205097392 U CN 205097392U CN 201520784767 U CN201520784767 U CN 201520784767U CN 205097392 U CN205097392 U CN 205097392U
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China
Prior art keywords
liquid material
twin
powder
pump
mill base
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CN201520784767.8U
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Chinese (zh)
Inventor
冯钦邦
王跃林
吴利民
段贤桂
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YICHANG KELIN SILICON MATERIALS CO., LTD.
Original Assignee
YICHANG KELIN SILICON MATERIALS Co Ltd
Guangzhou Daolin Synthetic Material Co Ltd
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Priority to CN201520784767.8U priority Critical patent/CN205097392U/en
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Abstract

The utility model discloses a silica gel mill base continuous production system, including the consecutive powder quantitative conveying device who connects of head and the tail, twin -screw grinder, grind the pump, the booster pump, a filte, cooler and partial shipment ware, powder to twin -screw grinder is carried to powder quantitative conveying device ration, parallelly connected first liquid material quantitative conveying device and the second liquid material quantitative conveying device who has independent separately ration transport liquid material of twin -screw grinder, twin -screw grinder forms powder and liquid material mixed grinding the mixture and carries the mixture to grinding in the pump attrition treatment once more, it carries the mixture and carries out pressure boost filtration treatment to booster pump and the filter in to grind the pump, twice ration of liquid material branch is carried and is increased the grinding pump and carry out follow -up attrition treatment, pressure boost filtration treatment device has been increased simultaneously, can be fine the fineness of pigment in the control silicon oil mill base, guarantee the homogeneity of silicon oil mill base, simultaneously the ration carries powder and liquid to expect to reduce material loss, guarantee product quality's stability simultaneously.

Description

A kind of silica gel mill base continuous process system
Technical field
The utility model relates to mill base production technical field, particularly a kind of mill base continuous process system.
Background technology
Mill base is a kind of pigment concentrate slurry, is to utilize different pigment, by technology such as surface of pigments process, surface parcels, develops through tight processing technology.At present, mill base is widely used in the industries such as fluid sealant, coating, adhesive tape, papermaking, toy, latex.
Chinese patent CN103230756B discloses a kind of continuous producing method and automatic assembly line of mill base, first by powder carry to powder meter; Then powder measured and to the powder of feeding machine continus convergence preset weight, then add liquid material to feeding machine, and powder and liquid material are mixed to get compound; Then compound is delivered to twin-screw main frame, then processes compound, the most backward twin-screw main frame adds adjustment liquid, obtains finished product.Although this production method effectively improves mill base production efficiency, obtain mill base by this production method and still there is the defects such as fineness is uneven, end product quality is unstable.
Utility model content
Technical problem to be solved in the utility model is to provide the silica gel mill base continuous process system that a kind of mill base uniformity is good, finished product is stable.
For solving the problems of the technologies described above adopted technical scheme: a kind of silica gel mill base continuous process system, comprise the quantitative powder conveying device that head and the tail are connected successively, twin-screw lapping device, grinding pump, booster pump, filter, cooler and dispenser, described quantitative powder conveying device quantitatively carries powder to twin-screw lapping device, described twin-screw lapping device is parallel with independent the first liquid material quantitative conveyer and the second liquid material quantitative conveyer of separately quantitatively carrying liquid material, powder and liquid material mixed grinding are formed compound and compound to be delivered in grinding pump milled processed again by described twin-screw lapping device, compound is delivered in booster pump and filter and carries out pressurizing filter process by described grinding pump again.
Further, described twin-screw lapping device is also connected with vacuum extractor compound being vacuumized to process.
Beneficial effect: in this silica gel mill base continuous process system, liquid material is quantitatively carried at twice and increased grinding pump and carries out follow-up milled processed, add pressurizing filter treating apparatus simultaneously, the fineness of pigment in silicone oil mill base can be controlled very well, ensure the uniformity of silicone oil mill base; Simultaneous quantitative conveying powder and liquid material can reduce material loss, ensure the stability of product quality simultaneously.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is described further;
Fig. 1 is the schematic diagram flow chart of the utility model silica gel mill base continuous process system.
Detailed description of the invention
A kind of silica gel mill base of the utility model continuous process system, comprise quantitative powder conveying device 10, twin-screw lapping device 30, grinding pump 50, booster pump 60, filter 70, cooler 80 and dispenser 90 that head and the tail are connected successively, twin-screw lapping device 30 is parallel with the first liquid material quantitative conveyer 21 and the second liquid material quantitative conveyer 22, and twin-screw lapping device 30 is also connected with vacuum extractor 40.
Quantitative powder conveying device 10 is for carry out powder quantitatively and to continus convergence in twin-screw lapping device 30.
First liquid material quantitative conveyer 21 and the second liquid material quantitative conveyer 22 are all for carry out powder quantitatively and respectively to continus convergence in twin-screw lapping device 30, wherein, first liquid material quantitative conveyer 21 is connected to twin-screw lapping device 30 front end, second liquid material quantitative conveyer 22 is connected to twin-screw lapping device 30 rear end, the first quantitatively transport portion liquid material of first liquid material quantitative conveyer 21 is in twin-screw lapping device 30, after the scheduled time of interval, second liquid material quantitative conveyer 22 more quantitatively transport portion liquid material in twin-screw lapping device 30, namely the first liquid material quantitative conveyer 21 and the second liquid material quantitative conveyer 22 separate twice conveying liquid material in twin-screw lapping device 30.
Twin-screw lapping device 30 forms mixed once material for carrying out preliminary mixed grinding process to powder and liquid material.
Vacuum extractor 40 is for removing moisture in mixed once material and bubble.
Grinding pump 50 forms secondary mixed material for carrying out follow-up milled processed to powder and liquid material, the transfer of the compound of formation, after the quantitative transport portion liquid material in twin-screw lapping device 30 rear end, to be delivered in grinding pump 50 milled processed again by the second liquid material quantitative conveyer 22.
Booster pump 60 obtains finished product for secondary mixed material pressure-increasing unit is carried out filtration treatment to filter 70.
Finished product is carried out cooling down process by cooler 80, so that subsequent treatment.
Dispenser 90 is for carrying out packing to finished product.
This silica gel mill base continuous process system is delivered in twin-screw lapping device 30 after being measured by quantitative powder conveying device 10, first liquid material quantitative conveyer 21 is also by liquid material metering and from twin-screw lapping device 30 front end charging aperture feeding screw rod lapping device 30, screw rod lapping device 30 pairs of liquid materials and powder mixes and pre-grinding process, vacuumize through vacuum extractor 40 pairs of compounds again, the moisture in removing compound and bubble; Quantitatively liquid material is carried to twin-screw lapping device 30 rear end charging aperture again, to control powder in compound and liquid material ratio by the second liquid material quantitative conveyer 22; Compound is delivered in grinding pump 50 again to carry out grinding and carry out pressure-increasing unit by booster pump 60 and filters in filter 70; Eventually pass cooler 80 and carry out cooling down, then pack through dispenser 90.
Wherein, liquid material carries out mixed grinding process with powder at twice, first time quantitatively adds part liquid material, make part powder and liquid material in twin-screw lapping device, first carry out premixed to grind and form mixed once material, first add part liquid material, powder content in compound can be improved, and then improve the viscosity of compound, strengthen shearing force, improve dispersion effect; After milled processed a period of time, in mixed once material, quantitatively add part liquid material for the second time and be delivered to grinding pump and carry out again mixed grinding formation secondary mixed material, second time quantitatively adds liquid material in order to control the ratio of liquid material and powder, the denseness of low silica gel mill base, and then the serviceability improving silica gel mill base.
The secondary mixed material formed in grinding pump carries out pressurizing filter process again, can control the fineness of pigment in silicone oil mill base further, ensures the uniformity of silicone oil mill base.
By reference to the accompanying drawings embodiment of the present utility model is explained in detail above, but the utility model is not limited to above-mentioned embodiment, in the ken that described technical field those of ordinary skill possesses, various change can also be made under the prerequisite not departing from the utility model aim.

Claims (2)

1. a silica gel mill base continuous process system, it is characterized in that: comprise the quantitative powder conveying device that head and the tail are connected successively, twin-screw lapping device, grinding pump, booster pump, filter, cooler and dispenser, described quantitative powder conveying device quantitatively carries powder to twin-screw lapping device, described twin-screw lapping device is parallel with independent the first liquid material quantitative conveyer and the second liquid material quantitative conveyer of separately quantitatively carrying liquid material, powder and liquid material mixed grinding are formed compound and compound to be delivered in grinding pump milled processed again by described twin-screw lapping device, compound is delivered in booster pump and filter and carries out pressurizing filter process by described grinding pump again.
2. silica gel mill base continuous process system according to claim 1, is characterized in that: described twin-screw lapping device is also connected with vacuum extractor.
CN201520784767.8U 2015-10-10 2015-10-10 Silica gel mill base continuous production system Active CN205097392U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520784767.8U CN205097392U (en) 2015-10-10 2015-10-10 Silica gel mill base continuous production system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520784767.8U CN205097392U (en) 2015-10-10 2015-10-10 Silica gel mill base continuous production system

Publications (1)

Publication Number Publication Date
CN205097392U true CN205097392U (en) 2016-03-23

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CN201520784767.8U Active CN205097392U (en) 2015-10-10 2015-10-10 Silica gel mill base continuous production system

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108857948A (en) * 2017-05-15 2018-11-23 深圳市二砂深联有限公司 A kind of mixing procedure of resin wheel

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108857948A (en) * 2017-05-15 2018-11-23 深圳市二砂深联有限公司 A kind of mixing procedure of resin wheel

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20190919

Address after: 443700 Economic Development Zone of Xingshan County, Yichang City, Hubei Province

Patentee after: YICHANG KELIN SILICON MATERIALS CO., LTD.

Address before: 510663 901A, four street, 10 science Avenue, Guangzhou, Guangdong, Luogang District

Co-patentee before: YICHANG KELIN SILICON MATERIALS CO., LTD.

Patentee before: GUANGZHOU DAOLIN SYNTHETIC MATERIAL CO., LTD.

TR01 Transfer of patent right