CN103908934A - Preparation apparatus for polyethylene wax micropowder - Google Patents
Preparation apparatus for polyethylene wax micropowder Download PDFInfo
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- CN103908934A CN103908934A CN201310634092.4A CN201310634092A CN103908934A CN 103908934 A CN103908934 A CN 103908934A CN 201310634092 A CN201310634092 A CN 201310634092A CN 103908934 A CN103908934 A CN 103908934A
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- reactor
- polyethylene wax
- thermocouple
- support
- preparation apparatus
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Abstract
The invention relates to a preparation apparatus for polyethylene wax micropowder. The preparation device comprises a reactor, a support, a thermocouple and a temperature monitor, wherein the reactor and the thermocouple are fixed on the support respectively; the thermocouple and the temperature monitor are connected for measuring a reaction temperature in the reactor. The preparation apparatus also comprises a furnace body. The reactor is disposed in the furnace body. The reactor is a cracking kettle. The support is provided with a rocking rod. The preparation apparatus for the polyethylene wax micropowder is simple in operations and short in flow, has no subsequent pollution and is controllable in particle size distribution, thereby showing wide application prospects for compound and development of novel functional materials.
Description
Technical field
The present invention relates to Tissuemat E production technical field, particularly polyethylene wax micro mist preparation facilities.
Background technology
That Tissuemat E has is nontoxic, non-corrosiveness, hardness is large, softening point is high, melting viscosity is low feature, has at normal temperatures good moisture resistance, chemical-resistant, electric property and antiwear heat resisting performance, and lubricity, dispersiveness, good fluidity.Its range of application is very extensive: in coating, add Tissuemat E can improve its surperficial anti-expansion performance, improve flatness, the scratch resistant of film and improve water proofing property, improve its hydrophily, play the effect of anti-skidding, prevent adhesion, spot-resistant; Tissuemat E can suitably be controlled the gloss of film, the Tissuemat E of different grain size and kind, and its extinction effect is not identical yet, from keeping gloss to deep dull completely, can allocate as required its consumption, thereby reach desirable effect; Tissuemat E is applied to Masterbatch processing, is not only to improve the processing characteristics of Masterbatch system, the more important thing is the dispersion that promotes pigment in Masterbatch.Tissuemat E can improve Pigments level to a certain extent, is conventional dispersant during Masterbatch is produced; Tissuemat E can change the mobility of ink for ink, improve hydrophily and printing performance, as regulated stickiness, makes ink loose and short; Accelerate set, make printing site complete, reduce the disadvantages such as set-off, epilation, caking.
In poly production process, can produce a small amount of oligomer is Low molecular weight polyethylene, claims again macromolecule wax, is called for short Tissuemat E.According to the difference of manufacture method, be divided into two kinds of aggretion type Tissuemat E and cracking type Tissuemat Es.The color of Tissuemat E mostly is white or faint yellow, and shape can need to be made bulk, sheet or Powdered according to difference.
Tissuemat E purposes is very extensive, particularly after micronization processes.The needs that can not meet at present market in the output of China's polyethylene wax micro mist far away, can only rely on a large amount of imports to supplement, and polyethylene micropowder can be used as fine chemical product and is widely used in each association area, and added value of product improves greatly.
Summary of the invention
Due to the restriction of technical merit, the production technology of the current Tissuemat E of China is also immature, and the indexs such as product appearance, particle diameter, fusing point, softening point and acid number can not reach technical requirement conventionally simultaneously, have limited its application.Improve product quality, it is more applied, still need and improve on production Technology and production equipment, in the hope of reaching internationalization level.
Polyethylene wax micro mist preparation facilities, it is characterized in that described device comprises reactor, support, thermocouple and temperature monitor, described reactor and thermocouple are separately fixed on support, and described thermocouple is connected with described temperature monitor, for the real time measure inside reactor reaction temperature.
Described device also comprises body of heater, and described reactor is placed in body of heater.
Described reactor is cracking still.
Described support is also provided with rocking bar.
Polyethylene wax micro mist preparation facilities of the present invention, because it is simple to operate, flow process is short, without plurality of advantages such as follow-up pollution, controllable granularity distribution of sizes, for the compound of new functional material and exploitation have represented wide application prospect.
Accompanying drawing explanation
Accompanying drawing 1 width of the present invention:
Fig. 1 is polyethylene wax micro mist preparation facilities schematic diagram of the present invention, in figure,
1 reactor; 2 bodies of heater; 3 rocking bars; 4 supports; 5 thermocouples; 6 temperature monitors;
The specific embodiment
Following non-limiting example can make the present invention of those of ordinary skill in the art's comprehend, but does not limit the present invention in any way.
Embodiment 1
Polyethylene wax micro mist preparation facilities, comprises reactor, support, thermocouple and temperature monitor, and described reactor and thermocouple are separately fixed on support, and described thermocouple is connected with described temperature monitor, for the real time measure inside reactor reaction temperature.Described device also comprises body of heater, and described reactor is placed in body of heater.Described reactor is cracking still.Described support is also provided with rocking bar.
Claims (4)
1. polyethylene wax micro mist preparation facilities, it is characterized in that described device comprises reactor, support, thermocouple and temperature monitor, described reactor and thermocouple are separately fixed on support, and described thermocouple is connected with described temperature monitor, for the real time measure inside reactor reaction temperature.
2. polyethylene wax micro mist preparation facilities according to claim 1, is characterized in that described device also comprises body of heater, and described reactor is placed in body of heater.
3. polyethylene wax micro mist preparation facilities according to claim 1, is characterized in that described reactor is cracking still.
4. polyethylene wax micro mist preparation facilities according to claim 1, is characterized in that described support is also provided with rocking bar.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310634092.4A CN103908934A (en) | 2013-11-28 | 2013-11-28 | Preparation apparatus for polyethylene wax micropowder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310634092.4A CN103908934A (en) | 2013-11-28 | 2013-11-28 | Preparation apparatus for polyethylene wax micropowder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103908934A true CN103908934A (en) | 2014-07-09 |
Family
ID=51035118
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310634092.4A Pending CN103908934A (en) | 2013-11-28 | 2013-11-28 | Preparation apparatus for polyethylene wax micropowder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103908934A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080131622A1 (en) * | 2006-12-01 | 2008-06-05 | White John M | Plasma reactor substrate mounting surface texturing |
| CN201912917U (en) * | 2010-11-17 | 2011-08-03 | 煤炭科学研究总院 | Micro high pressure reaction kettle experimental facility for directly liquefying coal |
| CN102952744A (en) * | 2011-08-31 | 2013-03-06 | 中国科学院过程工程研究所 | Biomass hydrothermal pretreatment reactor |
| CN103275335A (en) * | 2013-05-20 | 2013-09-04 | 安徽理工大学 | Preparation method of polyethylene wax micropowder and spray granulation system |
-
2013
- 2013-11-28 CN CN201310634092.4A patent/CN103908934A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080131622A1 (en) * | 2006-12-01 | 2008-06-05 | White John M | Plasma reactor substrate mounting surface texturing |
| CN201912917U (en) * | 2010-11-17 | 2011-08-03 | 煤炭科学研究总院 | Micro high pressure reaction kettle experimental facility for directly liquefying coal |
| CN102952744A (en) * | 2011-08-31 | 2013-03-06 | 中国科学院过程工程研究所 | Biomass hydrothermal pretreatment reactor |
| CN103275335A (en) * | 2013-05-20 | 2013-09-04 | 安徽理工大学 | Preparation method of polyethylene wax micropowder and spray granulation system |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20140709 |