CN1488665A - Colour master batch producing process - Google Patents
Colour master batch producing process Download PDFInfo
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- CN1488665A CN1488665A CNA03156089XA CN03156089A CN1488665A CN 1488665 A CN1488665 A CN 1488665A CN A03156089X A CNA03156089X A CN A03156089XA CN 03156089 A CN03156089 A CN 03156089A CN 1488665 A CN1488665 A CN 1488665A
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Abstract
The production process of colorant includes the following steps: 1). uniformly stirring polyethylene wax and color powder or filler; 2). cooling and caking; 3). pulverizing; and 4). extruding and granulating. The above-mentioned color powder can be organic one, also can be inorganic one. Said colorant has good dispersibility in plastics, and its production cost is low.
Description
1, technical field:
The present invention is a kind of production technique of Masterbatch, belongs to the innovative technology of Masterbatch production technique.
2, background technology:
At present China's Masterbatch technology of producing is to carry out putting the forcing machine extruding pelletization into after the high-speed stirring with molecular wax, plastic pellet or synthetic resin moulding compound and toner or stopping composition to form, because these materials begin to stir temperature just, therefore, plastics and molecular wax are difficult to coat each toner particle or stopping composition particle.The Masterbatch that this explained hereafter is come out is bad dispersibility in use, and there is the scar grain on the Masterbatch surface.For this reason, some producer uses other auxiliary agents, having coated each toner particle or filler grain, but needs cost a large amount of electric power energy and man-hour, causes the waste in the electricity charge and man-hour, has both increased production cost, has prolonged the production time again, the production efficiency of reduction.
3, summary of the invention:
The objective of the invention is to consider the problems referred to above and provide a kind of not only can reduce production costs, can shorten the production time again, the production technique of the Masterbatch of enhancing productivity.The Masterbatch of producing with production technique of the present invention is good dispersity in use, and the Masterbatch surface does not have the scar grain.
The production technique of Masterbatch of the present invention includes following steps:
1) polyethylene wax and toner or stopping composition are stirred;
2) cooling caking;
3) fragmentation;
4) extruding pelletization.
Above-mentioned steps 1) temperature of polyethylene wax can be 120 ℃~300 ℃ in.
Above-mentioned steps 2) adopts naturally cooling.
Above-mentioned steps 2) the naturally cooling time can be 20~40 minutes.
Above-mentioned steps 4) the extruding pelletization process in adopts hot water to extrude.
Above-mentioned hot water temperature can be 100 ℃~160 ℃.
Above-mentioned toner can be organic toner, also can be inorganic toner.
The present invention is owing to adopt molecular melt wax and the toner material of organic or inorganic or the complete processing that stopping composition stirs coating, therefore, it can guarantee that molecular melt wax coats each toner particle or stopping composition fully, it is dispersed fabulous that its Masterbatch of producing is applied in the plastics, the no scar grain in surface.The present invention not only can reduce production costs, and can shorten the production time again, enhances productivity, and is the production technique of a kind of simple and convenient, with low cost Masterbatch.
4, embodiment:
Embodiment:
The production technique of Masterbatch of the present invention includes following steps:
1) polyethylene wax and toner or stopping composition are stirred;
2) cooling caking;
3) fragmentation;
4) extruding pelletization.
Above-mentioned steps 1) polyethylene wax in obtains by the polyethylene cracking, and its temperature can be 120 ℃~300 ℃.The time that polyethylene wax and toner or stopping composition stir can be 30 seconds~and 30 minutes, decide according to what of concrete material and material, stir to guarantee material.Above-mentioned steps 2) adopt naturally cooling, the time can be 20~40 minutes, and in the present embodiment, the time of naturally cooling is 30 minutes.
Above-mentioned steps 4) the extruding pelletization process in adopts hot water to extrude, and the hot water temperature can be 100 ℃~160 ℃.In the present embodiment, the hot water temperature is 120 ℃.
Above-mentioned steps 1) toner in can be various natural colored raw materials, can be organic toner, also can be inorganic toner, and as carbon black, titanium dioxide etc., stopping composition can be lime carbonate, kaolin, talcum powder etc.
Claims (7)
1, a kind of production technique of Masterbatch is characterized in that including following steps:
1) polyethylene wax and toner or stopping composition are stirred;
2) cooling caking;
3) fragmentation;
4) extruding pelletization.
2, the production technique of Masterbatch according to claim 1 is characterized in that above-mentioned steps 1) in the temperature of polyethylene wax can be 120 ℃~300 ℃.
3, the production technique of Masterbatch according to claim 1 is characterized in that above-mentioned steps 2) the employing naturally cooling.
4, the production technique of Masterbatch according to claim 3 is characterized in that above-mentioned steps 2) the naturally cooling time can be 20~40 minutes.
5, the production technique of Masterbatch according to claim 1 is characterized in that above-mentioned steps 4) in the extruding pelletization process adopt hot water to extrude.
6, the production technique of Masterbatch according to claim 5 is characterized in that above-mentioned hot water temperature can be 100 ℃~160 ℃.
7,, it is characterized in that above-mentioned toner can be organic toner, also can be inorganic toner according to the production technique of claim 1 or 2 or 3 or 4 or 5 or 6 described Masterbatchs.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA03156089XA CN1488665A (en) | 2003-09-01 | 2003-09-01 | Colour master batch producing process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA03156089XA CN1488665A (en) | 2003-09-01 | 2003-09-01 | Colour master batch producing process |
Publications (1)
Publication Number | Publication Date |
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CN1488665A true CN1488665A (en) | 2004-04-14 |
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CNA03156089XA Pending CN1488665A (en) | 2003-09-01 | 2003-09-01 | Colour master batch producing process |
Country Status (1)
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CN (1) | CN1488665A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101033309B (en) * | 2006-03-09 | 2010-04-21 | 中国石油化工股份有限公司 | Color masterbatch for polythene and preparing method thereof |
CN102400236A (en) * | 2011-05-13 | 2012-04-04 | 上海容志材料科技有限公司 | Solid color master batch composite as well as preparation method and application thereof |
CN102888022A (en) * | 2012-10-18 | 2013-01-23 | 温州大洲无纺布有限公司 | Master batch and manufacturing method thereof |
CN103770238A (en) * | 2012-10-25 | 2014-05-07 | 上高骏造耐火材料有限公司 | Novel production technology for carrier-free plastic filled modified master batch |
-
2003
- 2003-09-01 CN CNA03156089XA patent/CN1488665A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101033309B (en) * | 2006-03-09 | 2010-04-21 | 中国石油化工股份有限公司 | Color masterbatch for polythene and preparing method thereof |
CN102400236A (en) * | 2011-05-13 | 2012-04-04 | 上海容志材料科技有限公司 | Solid color master batch composite as well as preparation method and application thereof |
CN102400236B (en) * | 2011-05-13 | 2014-08-27 | 上海容志材料科技有限公司 | Solid color master batch composite as well as preparation method and application thereof |
CN102888022A (en) * | 2012-10-18 | 2013-01-23 | 温州大洲无纺布有限公司 | Master batch and manufacturing method thereof |
CN103770238A (en) * | 2012-10-25 | 2014-05-07 | 上高骏造耐火材料有限公司 | Novel production technology for carrier-free plastic filled modified master batch |
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