CN1061028A - All purpose plastics packing parent grain and preparation method thereof - Google Patents
All purpose plastics packing parent grain and preparation method thereof Download PDFInfo
- Publication number
- CN1061028A CN1061028A CN 90102972 CN90102972A CN1061028A CN 1061028 A CN1061028 A CN 1061028A CN 90102972 CN90102972 CN 90102972 CN 90102972 A CN90102972 A CN 90102972A CN 1061028 A CN1061028 A CN 1061028A
- Authority
- CN
- China
- Prior art keywords
- weight
- filler
- turps
- polyethylene
- conditioning agent
- 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.)
- Pending
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
The present invention relates to all purpose plastics packing parent grain that a kind of thermoplastics uses and preparation method thereof.Easy to use by general purpose grade plastic master batch provided by the invention, the performance that can regulate plastics is improved its result of use, and reduces its cost greatly, is an important channel of improving plastic products quality at present.Carrier polyethylene that it is 1000-6000 by filler zeolite and white carbon black, molecular weight through micronizing to 1-20 μ and conditioning agent turps and white oil or oneself penta tetrol methyl esters form through the granulation of kneading.
Description
The present invention relates to filler for plastic, specifically, the present invention relates to all purpose plastics packing parent grain and preparation method thereof.
As everyone knows, the weighting agent of always continuing to use in the plastic working comprises such as lime carbonate, magnesiumcarbonate, talcum powder, potter's clay, kaolin, mica, asbestos and carbon black etc., but above-mentioned weighting agent can not satisfy the requirement that different plastics are adjusted product performance and improved result of use etc.
So, the purpose of this invention is to provide a kind of all purpose plastics packing parent grain and preparation method thereof, described plastic filler parent granule can be used among most of thermoplasticss, to improve physics, chemistry and the mechanical property of plastics.
The objective of the invention is to realize in the following manner: all purpose plastics packing parent grain that a kind of thermoplastics is used is characterized in that:
(1) fineness is that the filler of 1-20 μ comprises:
A) zeolite 30-40%(weight);
B) white carbon black 30-40%(weight);
(2) molecular weight is that the polyethylene support of 1000-6000 comprises:
C) polyethylene wax 20-40%(weight), and
(3) conditioning agent comprises:
D) turps 5-7%(weight)
E) white oil or oneself penta tetrol methyl esters 2.5-3.5%(weight).
It is characterized in that:
(1) described filler is that the filler of fineness 2-10 μ comprises:
A) zeolite 30-35%(weight);
B) white carbon black 30-35%(weight);
(2) described carrier is that the polyethylene of molecular weight 2000-3000 comprises
C) polyethylene wax 20-30%(weight), and
(3) conditioning agent comprises:
D) turps 6%(weight) and
E) white oil 2%(weight).
It is characterized in that described conditioning agent comprises:
D) turps 5%(weight) and
E) penta tetrol methyl esters 2.5%(weight).
And the preparation method of all purpose plastics packing parent grain that a kind of thermoplastics is used is characterized in that:
(1) filler is comprised:
A) zeolite 30-40%(weight), preferably be 30-35%(weight),
B) white carbon black 30-40%(weight), preferably be 30-35%(weight), the drying machine is ground into the fineness of 1-20 μ by supper micron mill after 100-120 ℃ of oven dry, be preferably the fineness of 2-10 μ.
(2) carrier is comprised:
C) the molecular weight 1000-6000 polyethylene 20-40%(weight of molecular weight 2000-3000 preferably), preferably be 20-30%(weight), in molten-bath in 105 °-110 ℃ be melt into liquid after, be added in the kneading machine, and keep the polyethylene liquid dissolve standby at 105 °-110 ℃.
(3) with the polyethylene wax carrier in the above-mentioned prescription in molten-bath in 105 °-110 ℃ be melt into liquid after, be added in the kneading machine, and remain on 105 °-110 ℃, with above-mentioned drying, filler after the pulverizing is zeolite and b a)) after white carbon black mixes, be added in the above-mentioned kneading machine in batches and mediate with polyethylene liquid, when adding 1/3 filler a) zeolite and b) behind the mixture of white carbon black, conditioning agent d with 1/2) and e) be added in the kneading machine, in 105 °-110 ℃ kneaded 30 minutes after, add 1/3 above-mentioned filler a) zeolite and b again) behind the miscellany of white carbon black, the above-mentioned conditioning agent d that will be left again) and e) add wherein, kneaded 30 minutes in 105 °-110 ℃ then, the 1/3 above-mentioned filler miscellany that then will be left again is added in the kneading machine, kneaded 1.5-2.5 hour in 105 °-110 ℃, be added in the container then, material is cooled to room temperature, carry out precomminution again and become irregular particle, extrude (extrusion temperature is 60 °-90 ℃) through forcing machine then, be cut into the particulate product of required specification again, be all purpose plastics packing parent grain of the present invention.
Advantage of the present invention is tangible, because the crystalline phase of zeolite itself is characterized as the bulk cavernous body of cross skeleton, when it and most of thermoplastics are admixed, need not to use coupling agent can with the closely embedding mutually of plastics polymer, and help to absorb liberated heat when solidifying, therefore improved the forming ability of plastics.White carbon black is as filler, and its major function is to give plastics with low water-absorbent and excellent dielectric properties, improves processing characteristics simultaneously.As for the selected polyethylene wax of the present invention as carrier, its advantage is that it and most of thermoplastics have consistency, therefore, the plastic filler parent granule of method preparation of the present invention can directly and after the fusion of thermoplastics particle carry out injection moulding, extrusion molding or blowing, have easy to usely, with low cost, can regulate the quality of plastics and improve its chemistry, physical and mechanical property.
Below, the present invention will be described in further detail by specific embodiment, so that advantage of the present invention is more obvious.
Embodiment:
One, prescription: (following all percentage ratio represent) by weight
(1) fineness be 1-20 μ, preferably for the filler of 2-10 μ, comprise
A) zeolite 30-40% preferably is 30-35%,
B) white carbon black 30-40% preferably is 30-35%,
(2) molecular weight be 1000-6000 preferably molecular weight be that the polyethylene support of 2000-3000 comprises:
C) polyethylene wax 20-40% preferably is 20-30%,
(3) conditioning agent comprises:
D) turps 5-7% preferably is 6% or 5%,
E) white oil or penta tetrol methyl esters 2.5-3.5% preferably be 2%-3% or 2.5%.
Two, preparation method:
(1) with the filler in the above-mentioned prescription a) zeolite and b) white carbon black respectively the drying machine in 100 ° of-120 ℃ of oven dry, in the supper micron mill that has 1-20 μ or 2-10 μ mesh screen, standby behind the separated pulverizing again;
(2) with the polyethylene wax carrier in the above-mentioned prescription in molten-bath in 105 °-110 ℃ be melt into liquid after, be added in the kneading machine, and remain on 105 °-110 ℃, with above-mentioned drying, filler after the pulverizing is zeolite and b a)) after white carbon black mixes, be added in the above-mentioned kneading machine in batches and mediate with polyethylene liquid, adding 1/3 filler a) zeolite and b) behind the miscellany of white carbon black, conditioning agent d with 1/2) and e) be added in the kneading machine, in 105 °-110 ℃ kneaded 30 minutes after, add 1/3 above-mentioned filler a) zeolite and b again) behind the mixture of white carbon black, the above-mentioned conditioning agent d that will be left again) and e) add wherein, kneaded 30 minutes in 105 ℃-110 ℃ then, the 1/3 above-mentioned filler miscellany that then will be left again is added in the kneading machine, kneaded 1.5-2.5 hour in 105 °-110 ℃, be added in the container then, material is cooled to room temperature, carry out precomminution again and become irregular particle, extrude (extrusion temperature is 60 °-90 ℃) through forcing machine then, be cut into the particulate product of required specification again, be all purpose plastics packing parent grain of the present invention.
Claims (6)
1, all purpose plastics packing parent grain used of a kind of thermoplastics is characterized in that:
(1) fineness is that the filler of 1-20 μ comprises:
A) zeolite 30-40% (weight),
B) white carbon black 30-40% (weight),
(2) polyethylene support of molecular weight 1000-6000 comprises:
C) polyethylene wax 20-40% (weight), and
(3) conditioning agent comprises:
D) turps 5-7% (weight),
E) white oil or penta tetrol methyl esters 2.5-3.5% (weight).
2, filler parent granule as claimed in claim 1 is characterized in that:
(1) described filler is that the filler of fineness 2-10 μ comprises:
A) zeolite 30-35%(weight),
B) white carbon black 30-35%(weight),
(2) described carrier is that the polyethylene of molecular weight 2000-3000 comprises
C) polyethylene wax 20-30%(weight), and
(3) conditioning agent comprises:
D) turps 6%(weight) and
E) white oil 3%(weight).
3, filler parent granule as claimed in claim 2 is characterized in that described conditioning agent comprises:
D) turps 5%(weight) and
E) oneself penta tetrol methyl esters 2.5%(weight).
4, the preparation method of all purpose plastics packing parent grain used of a kind of thermoplastics is characterized in that:
(1) filler is comprised:
A) zeolite 30-40%(weight),
B) white carbon black 30-40%(weight),
The drying machine is after 100 ° of-120 ℃ of oven dry, and the fineness that is ground into 1-20 μ by supper micron mill is standby;
(2) carrier is comprised:
C) molecular weight is the polyethylene 20-40%(weight of 1000-6000), in molten-bath in 105 °-110 ℃ be melt into liquid after, be added in the kneading machine, and keep fused polyethylene liquid standby at 105 °-110 ℃;
(3) filler with above-mentioned drying, after pulverizing: zeolite and white carbon black give earlier and mixing, and are added to then in the above-mentioned kneading machine to knead with polyethylene liquid in batches, after 1/3 filler adds, add 1/2 immediately:
(4) turps 5-7%(weight d)) and e) white oil or oneself penta tetrol methyl esters 2.5-3.5%(weight) conditioning agent, knead 105 °-110 ℃ of temperature of control then, after kneading 30 minutes, the d that adds 1/3 above-mentioned filler mixture and remaining 1/2 again), turps 5-7%(weight) and e) white oil or oneself penta tetrol methyl esters 2.5-3.5%(weight) conditioning agent, kneaded again 30 minutes, then, the 1/3 above-mentioned filler mixture that will be left again is added in the kneading machine, control is kneaded after 105 °-110 ℃ of temperature kneaded 1.5-2.5 hour, be added in the container then, be cooled to room temperature, carry out precomminution again and become irregular particle, extrude (extrusion temperature is from 60 °-90 ℃) through forcing machine then, be cut into the particulate product of required specification again.
5, method as claimed in claim 4 is characterized in that described filler preferentially adopts
(1) filler of 2-10 μ comprises:
A) zeolite 30-35%(weight),
B) white carbon black 30-35%(weight),
(2) described carrier is:
C) the polyethylene 20-30%(weight of molecular weight 2000-3000) and described (3) conditioning agent comprise:
D) turps 6%(weight) and
E) white oil 3%(weight).
6, method as claimed in claim 5 is characterized in that described (3) conditioning agent comprises:
D) turps 5%(weight) and
E) oneself penta tetrol methyl esters 2.5%(weight).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 90102972 CN1061028A (en) | 1990-10-29 | 1990-10-29 | All purpose plastics packing parent grain and preparation method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 90102972 CN1061028A (en) | 1990-10-29 | 1990-10-29 | All purpose plastics packing parent grain and preparation method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1061028A true CN1061028A (en) | 1992-05-13 |
Family
ID=4877842
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 90102972 Pending CN1061028A (en) | 1990-10-29 | 1990-10-29 | All purpose plastics packing parent grain and preparation method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1061028A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101173062B (en) * | 2007-10-23 | 2011-02-02 | 北京友合攀宝科技发展有限公司 | Antisepsis fresh-keeping master batch , producing method and application of the same |
| CN102070918A (en) * | 2009-11-19 | 2011-05-25 | 台州市黄岩明江塑胶有限公司 | Preparation method of calcium carbonate masterbatch |
| CN110229408A (en) * | 2019-07-02 | 2019-09-13 | 多华塑胶色料(深圳)有限公司 | A kind of universal white master batch and preparation method thereof |
-
1990
- 1990-10-29 CN CN 90102972 patent/CN1061028A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101173062B (en) * | 2007-10-23 | 2011-02-02 | 北京友合攀宝科技发展有限公司 | Antisepsis fresh-keeping master batch , producing method and application of the same |
| CN102070918A (en) * | 2009-11-19 | 2011-05-25 | 台州市黄岩明江塑胶有限公司 | Preparation method of calcium carbonate masterbatch |
| CN110229408A (en) * | 2019-07-02 | 2019-09-13 | 多华塑胶色料(深圳)有限公司 | A kind of universal white master batch and preparation method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR910003475B1 (en) | Prodection process of polyolefin resin composition containing inorganic filler | |
| DE69125965T2 (en) | Process for the production of a biodegradable, moldable material | |
| CN103275370A (en) | Ultraviolet light shielding, anti-bacterial, antifouling multifunctional color master batch and preparation method thereof | |
| JP2002220549A (en) | Granular inorganic filler and method for producing the same and resin composition compounded with the same | |
| BR9916087A (en) | Composition and process for rotary molding, process for producing a micropellet composition for rotational molding, use of a micropellet composition, rotationally molded polymer article and apparatus for the production of polyolefin pellets for rotational molding | |
| CN1215068A (en) | Stuffing mother particle for toughening polyolefine and preparation process and usage thereof | |
| US5028663A (en) | Solid state processing of polymer blends | |
| KR840007241A (en) | Granular Organic Halide Flame Retardant Additives | |
| CN103073771A (en) | Ultraviolet shielding, anti-bacterial and anti-fouling multifunctional color masterbatch and preparation method thereof | |
| EP0013872B1 (en) | A process for the production of particulate polyolefinic moulding materials containing conductive carbon black, and their use in the production of mouldings | |
| RU94044523A (en) | Freely flowing powder composition, method of preparation thereof, uniform layer produced from composition, carpet, container tape, and sealing means for bottle caps | |
| JPWO2004033538A1 (en) | Method for producing resin composition | |
| CN1061028A (en) | All purpose plastics packing parent grain and preparation method thereof | |
| JPH04129704A (en) | Production of polyarylene sulfide resin pellet | |
| CN2701614Y (en) | Device for preparing polymer composite additive | |
| JP3930613B2 (en) | Deodorant film material | |
| US5475059A (en) | Method of achieving superior dispersions of polymeric sulfur and products thereof | |
| KR0141421B1 (en) | Reproduction method of used rubber and used synthetic resin mixture | |
| CN1955220A (en) | Polyester resin composite and polyester resin medifier and resin molding | |
| CN1301300C (en) | Nanometer antibacterial sterilizing plastic mother material and preparing method thereof | |
| KR100564367B1 (en) | Olefin thermo plastic elastomer and process thereof | |
| EP3697863B1 (en) | Thermoplastic shape-stable polymer compositions for storing thermal energy | |
| JPH0337245A (en) | Granular rubber chemical | |
| JP2783427B2 (en) | Carbon fiber / thermoplastic compound | |
| CN1455796A (en) | Process for making thermoplastic molding compositions |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C01 | Deemed withdrawal of patent application (patent law 1993) | ||
| WD01 | Invention patent application deemed withdrawn after publication |