CN103788525A - Lubricating master batch for plastic processing and preparation method thereof - Google Patents

Lubricating master batch for plastic processing and preparation method thereof Download PDF

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Publication number
CN103788525A
CN103788525A CN201410044460.4A CN201410044460A CN103788525A CN 103788525 A CN103788525 A CN 103788525A CN 201410044460 A CN201410044460 A CN 201410044460A CN 103788525 A CN103788525 A CN 103788525A
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master batch
lubricant
plastic processing
vector resin
preparation
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CN201410044460.4A
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严兵
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Individual
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Individual
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Abstract

The invention provides lubricating master batch for plastic processing and a preparation method thereof. The lubricating master batch for plastic processing is prepared from the following components in parts by weight: 100 parts of matrix resin, 100 parts of filler with a lubricating effect, 3-10kg of various lubricants for plastic processing and 0.1-0.5 parts of antioxidant. The lubricating master batch for plastic processing is prepared to spherical, columnar particles and the like by virtue of extrusion and prilling. The lubricating master batch for plastic processing can be used as a lubricant for modifying and processing a macromolecular material and is convenient to add and accurate to meter, uniformly to mix in kneading process and convenient in effect taking during a process of modifying and processing a macromolecular material.

Description

A kind of lubricated master batch and preparation method thereof for plastic working
Technical field
The present invention relates to field of high polymer material processing, be specially lubricated master batch and preparation method thereof for a kind of plastic working.
Background technology
The development of macromolecular material is advanced by leaps and bounds in recent decades, and the processing modified of macromolecular material grows up in order to meet the particular requirements such as automobile, electrical equipment, communication, high-grade instrument.Single macromolecular material is often because certain some defect is difficult to meet the demands.And will make its performance increase substantially by carrying out modification with other macromolecular materials or packing material, meet different requirements.
And in the processing modified process of macromolecular material, need different processing aids to coordinate, wherein lubricant is exactly very important one.The Main Function of lubricant is exactly the friction reducing in the course of processing between macromolecular material and processor surface, macromolecular material interior molecules, thereby improves its processibility, and improves the performance of macromolecular material.Lubricant mainly contains hydro carbons (as paraffin), aliphatic acid (as stearic acid) and acid amides are (as stearic amide, N, the higher stearic amide of fusing point of N-ethylene bis stearic acid amide and modification), ester class (as Chinese wax, stearate) and salt (stearate), higher alcohols (C18 alcohol, C16 alcohol), low-molecular-weight polyolefin (polyethylene wax, oxidized polyethlene wax), organosilicon (silicone oil, silicone) etc.From lubricant role, can be divided into again internal lubricant, external lubricant or early stage lubricant, later stage lubricant.Therefore in use in order to keep lubrication balance, often need multiple lubricant compound use.
Most lubricants are all powderies, and most resin particle is circular or oval, and the amount of lubricant accounts for a little part in plastic composite.Therefore in the course of processing, powder can spill between the gap of particle, causes inhomogeneous.Not only cannot better bring into play the effect of lubricant, and local too much, the detrimentally affect such as also can cause that lubricant is separated out.
Plastic master batch is widespread use in plastic working modification, and as Masterbatch, fire-retardant master granule, filling master batch and other functional agglomerates, but lubricated master batch research is few.
Patent CN103044740A introduces the lubricated master batch of a kind of filling plastic, and the lubricated master batch of this invention filling plastic is by 100 parts of inorganic powders by mass, 20~100 parts of lubricants, 1~5 lubrication assistant dispersion agent, 0.1~3 part of coupling agent, the vector resin of 5~30 parts, 0~2 part of compound particle that forms of functional agent.This patent is preferred by raw material, by compound to sheet and spherical inorganic powder, coordinate again other components, the packing lubrication master batch forming has good oilness and fills increment effect in plastic working, have toughness reinforcing enhancing concurrently, increase the effects such as glossiness, reach the object that packing lubrication unites two into one, be conducive to simplify plastic formula and technique, improve plastics over-all properties, reduce production costs.But the main object of this patent is as filling master batch, so filler accounts for the overwhelming majority, and oilness is an auxiliary function.
Summary of the invention
The invention provides lubricated master batch and preparation method thereof for a kind of plastic working, this masterbatch melts finger vector resin with height, be used for wrapping up one or several lubricants, suitably add other compositions and processing aid, then mix, utilize Banbury mixer, screw extrusion press etc. to carry out granulation, obtain lubricated master batch.The benefit of this lubricated master batch is good and resin particle mixes, and better brings into play its effect.
Lubricant can be hydro carbons (as paraffin), aliphatic acid (as stearic acid) and acid amides are (as stearic amide, N, the higher stearic amide of fusing point of N-ethylene bis stearic acid amide and modification), ester class (as Chinese wax, stearate) and salt (stearate), higher alcohols (C18 alcohol, C16 alcohol), low-molecular-weight polyolefin (polyethylene wax, oxidized polyethlene wax), organosilicon (silicone oil, silicone) etc.For the lower polyolefine of processing temperature, can select the lubricant that fusing point is lower.And the higher engineering plastics of processing temperature need to be selected the higher lubricant of fusing point.And in actual use, need the composite use of multiple lubricant.The polyolefine such as EVA, POE, PE, PP that can adopt for the lubricant using in polyolefine material, as vector resin, is prepared lubricated master batch.Select to refer to be chosen in 5-50 as polyolefinic the melting of vector resin, the material referring at 20-30 is melted in preferential selection.Can adopt high PS, the PA etc. that melts finger as vector resin for the lubricant using in engineering plastics, prepare lubricated master batch.Select to refer to be chosen in 5-50 as PS, ABS, the melting of PA of vector resin, the material referring at 10-20 is melted in preferential selection.And for needing heating adding of lubricated master batch, therefore add a certain amount of oxidation inhibitor.Oxidation inhibitor can be selected conventional oxidation inhibitor and combination, preferential 1010 or 168 and combination.For the lower material of intensity, can add a small amount of filler, filler is preferentially selected talcum powder.
Technical scheme of the present invention, provides lubricated master batch and preparation method thereof for a kind of plastic working, is wherein made up of vector resin, lubricant compositions, oxidation inhibitor.Vector resin is to melt polyolefine, PS, the PA etc. that finger is higher, and Lubrication Composition is multiple lubricant compositions, and oxidation inhibitor is one or more compositions.Vector resin in lubricated master batch: Lubrication Composition: oxidation inhibitor is (10~40): (50~70): (1~10).
Embodiment
The object of this invention is to provide lubricated master batch and preparation method thereof for a kind of plastic working.This masterbatch melts finger vector resin with height, for wrapping up one or several lubricants, suitably adds other compositions and processing aid, then mixes, and utilizes Banbury mixer, screw extrusion press etc. to carry out granulation, obtains lubricated master batch.Be embodiment below, can further understand technical solution of the present invention by them.But the present invention does not limit to so, every of the present invention being equal to or equivalent transformation,, all in protection scope of the present invention.
Embodiment 1:
Batching: DF820020kg, SA20kg, paraffin 30kg, polyethylene wax 20kg, antioxidant 1010 2kg, irgasfos 168 2kg, talcum powder 10kg.
Mix: above-mentioned material stirs 3-5 minute in mixing kettle, mixes.
Granulation: by the material mixing, utilize twin screw extruder granulation, technological temperature is at 60-90 ℃.
Embodiment 2:
Batching: EVA26520kg, ethylene bis stearic acid amide (EBS) 30kg, paraffin 10kg, polyethylene wax 30kg, antioxidant 1010 2kg, irgasfos 168 2kg, talcum powder 10kg.
Mix: above-mentioned material stirs 3-5 minute in mixing kettle, mixes.
Granulation: by the material mixing, utilize twin screw extruder granulation, technological temperature is at 60-90 ℃.
Embodiment 3:
Batching: PP Z30S30kg, ethylene bis stearic acid amide (EBS) 30kg, Zinic stearas 10kg, polyethylene wax 20kg, antioxidant 1010 2kg, irgasfos 168 2kg, talcum powder 10kg.
Mix: above-mentioned material stirs 3-5 minute in mixing kettle, mixes.
Granulation: by the material mixing, utilize twin screw extruder granulation, technological temperature is at 180-220 ℃.
Embodiment 4:
Batching: ABS-756H40kg, TAS-2A (modification EBS) 40kg, polyethylene wax 10kg, antioxidant 1010 2kg, irgasfos 168 2kg, talcum powder 10kg.
Mix: above-mentioned material stirs 3-5 minute in mixing kettle, mixes.
Granulation: by the material mixing, utilize twin screw extruder granulation, technological temperature is at 220-260 ℃.
Embodiment 5:
Batching: PA61013GH3040kg, TAF (modification EBS, purchased from Suzhou Xingtai state light) 50kg, polyethylene wax 10kg, antioxidant 1010 2kg, irgasfos 168 4kg.
Mix: above-mentioned material stirs 3-5 minute in mixing kettle, mixes.
Granulation: by the material mixing, utilize twin screw extruder granulation, technological temperature is at 220-260 ℃.

Claims (5)

1. lubricated master batch for a kind of plastic working of preparation, containing vector resin, one or several lubricants, processing aid.
2. according to claim 1, vector resin is selected polyolefine, melts and refers to be chosen in 5-50, and the material referring at 20-30 is melted in preferential selection.
3. according to claim 1, vector resin is selected PS, ABS, PA, melts and refers to be chosen in 5-50, and the material referring at 10-20 is melted in preferential selection.
4. according to claim 1, lubricant is hydro carbons (as paraffin), aliphatic acid (as stearic acid) and acid amides are (as stearic amide, N, the higher stearic amide of fusing point of N-ethylene bis stearic acid amide and modification), ester class (as Chinese wax, stearate) and salt (stearate), higher alcohols (C18 alcohol, C16 alcohol), low-molecular-weight polyolefin (polyethylene wax, oxidized polyethlene wax), organosilicon (silicone oil, silicone).It can be the mixture of one or several wherein.
5. according to claim 1, oxidation inhibitor can be selected conventional oxidation inhibitor and combination, preferential 1010 or 168 and combination.
CN201410044460.4A 2014-01-24 2014-01-24 Lubricating master batch for plastic processing and preparation method thereof Pending CN103788525A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106543618A (en) * 2016-11-03 2017-03-29 苏州兴泰国光化学助剂有限公司 AS multifunctional transparents lubricate master batch
CN109090805A (en) * 2018-08-25 2018-12-28 广东麒麟精工科技有限公司 The Oil-free middle bundle core of plastic shaping
CN110684258A (en) * 2018-07-05 2020-01-14 成都盛腾科技发展有限公司 Polyethylene modified material and preparation method thereof
CN113512292A (en) * 2021-05-14 2021-10-19 宝新高分子科技(广州)有限公司 Lubricating composition, low-smoke halogen-free material and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102643507A (en) * 2012-05-10 2012-08-22 金发科技股份有限公司 Extremely-high-temperature-resistant anti-flaming ABS (Acrylonitrile Butadiene Styrene) composition as well as preparation method and applications thereof
CN102643489A (en) * 2012-05-07 2012-08-22 青岛国恩科技股份有限公司 Flame-retarding toughening polystyrene master batch and preparation method thereof
CN102838828A (en) * 2011-06-20 2012-12-26 上海安凸塑料添加剂有限公司 Bright-black functional black masterbatch for ABS engineering plastics and preparation method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102838828A (en) * 2011-06-20 2012-12-26 上海安凸塑料添加剂有限公司 Bright-black functional black masterbatch for ABS engineering plastics and preparation method thereof
CN102643489A (en) * 2012-05-07 2012-08-22 青岛国恩科技股份有限公司 Flame-retarding toughening polystyrene master batch and preparation method thereof
CN102643507A (en) * 2012-05-10 2012-08-22 金发科技股份有限公司 Extremely-high-temperature-resistant anti-flaming ABS (Acrylonitrile Butadiene Styrene) composition as well as preparation method and applications thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106543618A (en) * 2016-11-03 2017-03-29 苏州兴泰国光化学助剂有限公司 AS multifunctional transparents lubricate master batch
CN110684258A (en) * 2018-07-05 2020-01-14 成都盛腾科技发展有限公司 Polyethylene modified material and preparation method thereof
CN109090805A (en) * 2018-08-25 2018-12-28 广东麒麟精工科技有限公司 The Oil-free middle bundle core of plastic shaping
CN109090805B (en) * 2018-08-25 2021-04-30 广东麒麟精工科技有限公司 Oil-free middle bundle core formed by plastic
CN113512292A (en) * 2021-05-14 2021-10-19 宝新高分子科技(广州)有限公司 Lubricating composition, low-smoke halogen-free material and preparation method thereof

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Application publication date: 20140514