CN1230481A - Preparation of foamed insulating polyethylene material for coaxial cable - Google Patents

Preparation of foamed insulating polyethylene material for coaxial cable Download PDF

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Publication number
CN1230481A
CN1230481A CN 98111927 CN98111927A CN1230481A CN 1230481 A CN1230481 A CN 1230481A CN 98111927 CN98111927 CN 98111927 CN 98111927 A CN98111927 A CN 98111927A CN 1230481 A CN1230481 A CN 1230481A
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Prior art keywords
coaxial cable
nucleator
preparation
foamed insulating
10min
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CN 98111927
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CN1098761C (en
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吴廷禄
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Sichuan Union University
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Sichuan Union University
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Abstract

The present invention relates to the field of plastic processing and application. The foamed insulating material is prepared by using the material including high density polyethylene with melt index of 3-9 g/10min, low density polyethylene with melt index of 0.2-2 g/10min and nucleating agent and through intermingling, smelting to extrude and pelletizing. The coaxial cable with the foamed insulating material has excellent performance of characteristic impedance, echo loss, insulation resistance, attenuation loss, etc. The foamed insulating material is comparable to imported physical foamed insulating material for coaxial cable.

Description

Preparation of foamed insulating polyethylene material for coaxial cable
The present invention relates to plastic processing technology, belong to the used preparation of foamed insulating polyethylene material of coaxial cable physical blowing.
In the prior art, coaxial cable cellular insulation material manufacture method has two kinds: a kind of is by the direct synthetic foam Insulation Material of resin production plant, another kind is to form with high density polyethylene (HDPE) (HDPE) resin and the direct blending of low density polyethylene (LDPE) (LDPE) resin, and the coaxial cable producer is blending nucleator (CBA) more in use.Preceding a kind of method, because equipment investment is huge, the synthetic technology complexity, the product market price costliness, the CABLE MATERIALS production supplier of countries in the world seldom adopts.A kind of method in back is that the cable production supplier of countries in the world generally adopts, as U.S. Quantum Chemical Corp, the said firm is the main supplier of coaxial cable insulation cable material, the coaxial cable cellular insulation material that the provides preparation that comes to this.Promptly use HDPE (LS6081-00) resin and LDPE (NA951-000) resin to make in the direct blend of 1: 3~3: 1 ratio.And for example the Japan Patent spy opens the cellular insulation preparation method for material that tire 58-223210 discloses, and also belongs to this method.The concrete preparation method of this patent is, is that 80~97% HDPE resin and percentage by weight are 3~20% the direct blend of LDPE resin with percentage by weight, promptly makes Insulation Material.Wherein the density of HDPE (ρ) is 0.940~0.96g/cm 3, melt index (MI) (Mi) is 0.3~2g/10min; The density of LDPE (ρ) is 0.921~0.934g/cm 3, melt index (MI) (Mi) is less than 1.0g/10min.
Although a kind of method in back generally adopts for countries in the world cable insulating material production supplier, but still exist the place of some shortcomings.One prepares cable insulating material with HDPE resin and the direct according to a certain percentage blend of LDPE resin, and its mixing belongs to the solid mechanical mixture, and two kinds of mixed with resin are inhomogeneous.With mixing the cable insulation that uneven Insulation Material foaming is extruded, its surface smoothness and fineness are all relatively poor, and the cable footpath is wayward, and mutual capacitance is also unstable.It two is not contain nucleator in the Insulation Material, and nucleator is mixed voluntarily in proportion by the cable producer, uses inconvenient.Because it is not the foaming effect of the addition direct relation cable fluid insulation of nucleator is a key factor that influences cable quality, punctual again when the nucleator ratio that cables manufacturing person mixes voluntarily, will influence the foam quality of coaxial cable.Severe patient can make the foamed cable report from a liner of extruding useless, causes very big economic loss.
The method that the purpose of this invention is to provide a kind of simple and easy to do manufacturing coaxial cable polyethylene foam insulation material that HDPE, LDPE and CBA are combined together, process the coaxial cable of extruding with the Insulation Material that the present invention produces, its polyethylene foam insulation layer, surfacing is bright and clean, the control easily of line footpath, good electrical property, and the user uses very convenient.
Coaxial cable cellular insulation material performance requirement is higher, not only require to have good processing properties, so that when extrusion foaming, be easy to control line footpath, mutual capacitance and foam degrees, also good electrical properties will be arranged, the cable of promptly making will have good characteristic impedance, return loss, insulaion resistance, attenuation constant etc.Except that above-mentioned requirements, good mechanical performance and nucleation performance to be arranged also.Any at present resin all can not satisfy these requirements all sidedly.Blending and modifying is the effective ways that satisfy the above-mentioned performance of cellular insulation material.The inventor is based upon to carry out technical conceive on such basis, improves blend method to realize the above-mentioned purpose of invention.
As follows in order to realize the object of the invention technical scheme:
It with percentage by weight 40~80% high density polyethylene (HDPE) (HDPE) resin, 5~50% low density polyethylene (LDPE) (LDPE) resin and 0.03~0.05% nucleator are raw material, blending under solid state earlier, fully mixing under molten condition then, the back extruding pelletization makes it to combine together, make the cellular insulation material, the operating temperature of melting mixing extrusion is controlled at and is not higher than 180 ℃.The antioxidant that in the melting mixing process, also can add raw material total amount 0.05~0.1% (weight).The nucleator that preferably contains the activator composition as the nucleator of one of raw material components.The kind of nucleator is a lot, as Celogen Az; Azoformic acid barium; N, N '-subunit five methine tetramines etc.Antioxidant can be four (3-(3 ', 5 ')-di-t-butyl-4 '-hydroxy phenyl) propionic acid pentaerythritol ester; 1,1,3-three (2-methyl-4-hydroxyl-5-tert-butyl-phenyl) butane; 2,2 ' one dihydroxy-3,3 '-two (Alpha-Methyl cyclohexyl)-5,5 '-dimethyl diphenylmethane; 4,4 '-methylene bis (2, the 6-DI-tert-butylphenol compounds) etc.Activator can be a metal oxide, as zinc oxide, aluminium oxide etc.; Also can be stearate, as stearic acid every, zinc stearate, barium stearate etc.; Can also be nonmetallic compound, as glycerine, diethylene glycol etc.High density polyethylene (HDPE) (HDPE) as raw material can select density at 0.940~0.960g/cm 3, melt index (MI) is between the 3-9g/10min; Low density polyethylene (LDPE) (LDPE) can select density at 9.10~0.925g/cm 3, melt index (MI) is between 0.2~0.25g/10min; It is 190~210 ℃ that nucleator (CBA) can be selected decomposition temperature, and fineness is not less than 200 purposes.Preferably selecting melt index (MI) is the HDPE of 6~8g/min, and melt index (MI) is the LDPE of 1.5~2g/10min, the CBA that decomposition temperature is 195~205 ℃.
Compared with the prior art the present invention has following relatively more outstanding advantage:
1. the present invention is with raw material HDPE resin, the blend under solid state earlier of LDPE resin and nucleator, and then it is fully mixing under molten condition, they are combined together, extruding pelletization prepares Insulation Material, with the Insulation Material of HDPE resin and the direct blend preparation of LDPE resin, the mixing of blend is very even compared to prior art.The coaxial cable insulated layer of manufacturing is extruded in Insulation Material foaming with the present invention's preparation, and its surfacing is bright and clean, and the insulating barrier presentation quality is very good.
2. the Insulation Material of prior art for preparing does not contain nucleator, and nucleator, is blended in the Insulation Material when producing cable by the Insulation Material user, disperses inhomogeneous.And the Insulation Material of the present invention's preparation has contained nucleator, and nucleator is by the solid blend, and melting mixing very is evenly dispersed in the resin.Insulating barrier is made in Insulation Material foaming with the present invention preparation, can obtain abscess densification, high-quality foaming body that all even foam degrees is high.Simultaneously also can avoid adding nucleator more in addition, and because the user adds the inaccurate quality accident that causes of ratio of nucleator voluntarily, and the user uses more convenient, quality is also more secure by the user.
3. the nucleator that uses of the present invention, it is the nucleator that contains the activator composition, the decomposition temperature of nucleator is low, therefore, when making coaxial cable insulated layer with the Insulation Material of the present invention's preparation, nucleator decomposes more abundant more fully, and decompose residues is almost 0, eliminated the corrosion of residue, improved the cable transmission effect the cable copper cash.
The present invention also has more otherwise advantages.
Of the present invention open, for people provide a kind of technology simple, realize easily, raw material sources are extensive, and production cost is low, the cable cellular insulation material production technology that economic benefit is considerable, and the cellular insulation material of preparation has contained finely dispersed nucleator, uses very convenient.Its performance can satisfy the coaxial cable physical blowing to the requirement of polyethylene foam insulation material all properties.With the direct blend Insulation Material of the Insulation Material substituting import one of the present invention preparation, per tonly economize on the use of funds 2000 yuan.
Two embodiment of the present invention are disclosed below:
Embodiment 1:
Density is 0.954g/cm 3, melt index (MI) is 6.5g/10min, consumption is the HDPE resin of 70% (weight); Density is 0.918g/cm 3Melt index (MI) is 1.8g/10min, consumption is that the LDPE resin and the molecular weight of 29.85% (weight) is 116, fineness is by 200 orders, gas forming amount is 285ml/g, decomposition temperature is 195 ℃, consumption is 0.05% (weight), and the Celogen Az nucleator that contains the zinc oxide activator earlier directly carries out blending, add again total amount 0.1% (weight) four (3-(3,5 ')-and di-t-butyl-4 '-hydroxy phenyl) propionic acid pentaerythritol ester antioxidant, be heated to 175 ℃, and then move into double screw extruder, fully mixing under molten condition, make its back extruding pelletization that combines together, promptly obtain coaxial cable physical blowing HDPE (high density polyethylene) cellular insulation material.Its performance such as subordinate list 1.
Embodiment 2:
Density is 0.954g/cm 3, melt index (MI) is 6.5g/10min, consumption is the HDPE of 50% (weight); Density is 0.918g/cm 3Melt index (MI) is 1.8g/10min, consumption is that the LDPE and the molecular weight of 49.95% (weight) is 116, fineness is by 200 orders, gas forming amount is 285mp/g, 195 ℃ of decomposition temperatures, consumption are 0.05% (weight), contain stearic acid and directly carry out earlier blending every the nucleator of the azoformic acid barium of activator, add total amount again and be 0.1% (weight) 1,1,3-three (2-methyl-4-hydroxyl-5-tert-butyl-phenyl) butane antioxidant moves in the double screw extruder then, under 175 ℃ of conditions, melt extrude granulation, promptly obtain coaxial cable physical blowing MDPE (Medium-density polyethylene) cellular insulation material, its performance such as subordinate list 1.
Table 1 polyethylene foam insulation material of the present invention performance
Sequence number Project name Unit Embodiment 1 Embodiment 2
????1 Melt flow rate (MFR) ????g/10min ????4.8 ????3.1
????2 Density ????g/cm 3 ????0.951 ????0.939
????3 Black brittleness-76 ℃ Failure number ????0/10 ????0/10
????4 The anti-yield strength of stretching ????Mpa ????20.5 ????18.6
????5 Elongation at break ????% ????528 ????519
????6 Oxidation induction period ????min ????55 ????61
????7 Dielectric constant 1MH2 ????2.30 ????2.31
????8 Dielectric dissipation factor 1MHZ ??2.1×10 -4 ?1.9×10 -4
????9 Specific insulation ????Ω.m ??4.5×10 13 ?4.6×10 13
???10 Frothing percentage ????% ????50 ????49
???11 Expanded beads number Grain/50g ????0 ????0

Claims (5)

1. preparation of foamed insulating polyethylene material for coaxial cable, it is characterized in that high density polyethylene (HDPE) with 40~80% (weight), the nucleator of the low density polyethylene (LDPE) of 5~59% (weight) and 0.03~0.05% (weight) is a raw material, blending under solid state earlier, abundant mixing combining together under molten condition then, extruding pelletization, melting mixing extrusion temperature are not higher than 180 ℃.
2. preparation of foamed insulating polyethylene material for coaxial cable according to claim 1 is characterized in that in melt extruding process adding the antioxidant of raw material total amount 0.05~0.1% (weight).
3. preparation of foamed insulating polyethylene material for coaxial cable according to claim 1 and 2 is characterized in that nucleator is the nucleator that contains activator.
4. preparation of foamed insulating polyethylene material for coaxial cable according to claim 3, the density that it is characterized in that said high density polyethylene (HDPE) is 0.940~0.960g/cm 3, melt index (MI) is 3-9g/10min; The density of low density polyethylene (LDPE) is 0.910~0.925g/cm 3, melt index (MI) is 0.2~2.5g/10min; The decomposition temperature of nucleator is 190~210 ℃, and fineness is not less than 200 orders.
5. coaxial cable polyethylene foam insulation material according to claim 4, the melt index (MI) that it is characterized in that high density polyethylene (HDPE) is 6~8g/10min, and the melt index (MI) of low density polyethylene (LDPE) is 1.5~2g/10min, and the nucleator decomposition temperature is 195~205 ℃.
CN98111927A 1998-03-31 1998-03-31 Preparation of foamed insulating polyethylene material for coaxial cable Expired - Fee Related CN1098761C (en)

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Cited By (12)

* Cited by examiner, † Cited by third party
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CN100354987C (en) * 2005-08-30 2007-12-12 上海乐庭电子线缆有限公司 Method for fabricating fire resistant communication cable, and products
CN102627794A (en) * 2012-03-28 2012-08-08 天津市普立泰高分子科技有限公司 Physical foaming polyethylene insulating material and preparation method thereof
CN103035331A (en) * 2012-12-13 2013-04-10 苏州亨利通信材料有限公司 Anti-moisture filling rope and manufacturing process of anti-moisture filling rope
CN103030860A (en) * 2012-12-13 2013-04-10 苏州亨利通信材料有限公司 Foaming filler yarn granule for optical cable and preparation process thereof
CN103035330A (en) * 2012-12-13 2013-04-10 苏州亨利通信材料有限公司 Foaming filler yarn applied to optical cable and preparation process of the same
CN101633757B (en) * 2009-08-27 2013-05-01 杭州临安光大线缆有限公司 Method for preparing coaxial cable core wire foaming insulation layer composition
CN103113653A (en) * 2013-02-06 2013-05-22 常州大学 HDPE (high-density polyethylene)/LDPE (low-density polyethylene) blended foam material and preparation method thereof
CN104166198A (en) * 2012-12-13 2014-11-26 苏州亨利通信材料有限公司 Manufacturing method of high-strength foaming filler rope
CN104693581A (en) * 2012-12-13 2015-06-10 苏州亨利通信材料有限公司 Granular filling rope material for anti-deformation cable
CN104698555A (en) * 2012-12-13 2015-06-10 苏州亨利通信材料有限公司 Manufacturing process of low-expansion fillings for optical cables
CN105469867A (en) * 2015-12-16 2016-04-06 江苏亨通线缆科技有限公司 Special cable for wear-resistant locomotive vehicle
CN105551585A (en) * 2015-12-16 2016-05-04 江苏亨通线缆科技有限公司 High-strength high-fire-retardance locomotive cable

Family Cites Families (4)

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CN1008750B (en) * 1988-12-23 1990-07-11 杨景德 The production method of high-strength polyethylene netting twine
CN1036596C (en) * 1992-02-18 1997-12-03 中国石化齐鲁石油化工公司 Special material for polyethylene fuel tank of automobile and preparation method thereof
US5574074A (en) * 1993-02-19 1996-11-12 Mitsubishi Cable Industries, Inc. Foamable organic polymer composition and production of foamed article
CN1124258A (en) * 1994-12-09 1996-06-12 天水电缆材料厂 Black polyvinyl cable material and producing technology

Cited By (21)

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Publication number Priority date Publication date Assignee Title
CN100354987C (en) * 2005-08-30 2007-12-12 上海乐庭电子线缆有限公司 Method for fabricating fire resistant communication cable, and products
CN101633757B (en) * 2009-08-27 2013-05-01 杭州临安光大线缆有限公司 Method for preparing coaxial cable core wire foaming insulation layer composition
CN102627794A (en) * 2012-03-28 2012-08-08 天津市普立泰高分子科技有限公司 Physical foaming polyethylene insulating material and preparation method thereof
CN104693581A (en) * 2012-12-13 2015-06-10 苏州亨利通信材料有限公司 Granular filling rope material for anti-deformation cable
CN103035331B (en) * 2012-12-13 2015-08-26 苏州亨利通信材料有限公司 Water vapor gasket for packing and manufacturing process thereof
CN103030860A (en) * 2012-12-13 2013-04-10 苏州亨利通信材料有限公司 Foaming filler yarn granule for optical cable and preparation process thereof
CN104698555B (en) * 2012-12-13 2019-02-05 苏州亨利通信材料有限公司 The manufacturing process of optical cable low bulk filler material
CN104166198A (en) * 2012-12-13 2014-11-26 苏州亨利通信材料有限公司 Manufacturing method of high-strength foaming filler rope
CN103030860B (en) * 2012-12-13 2015-04-29 苏州亨利通信材料有限公司 Foaming filler yarn granule for optical cable and preparation process thereof
CN105367865B (en) * 2012-12-13 2018-10-30 苏州亨利通信材料有限公司 The preparation process of low-expansion coefficient polyethylene foam gasket for packing
CN103035331A (en) * 2012-12-13 2013-04-10 苏州亨利通信材料有限公司 Anti-moisture filling rope and manufacturing process of anti-moisture filling rope
CN104698555A (en) * 2012-12-13 2015-06-10 苏州亨利通信材料有限公司 Manufacturing process of low-expansion fillings for optical cables
CN103035330A (en) * 2012-12-13 2013-04-10 苏州亨利通信材料有限公司 Foaming filler yarn applied to optical cable and preparation process of the same
CN105367865A (en) * 2012-12-13 2016-03-02 苏州亨利通信材料有限公司 Preparation technology of low-expansion-coefficient polyethylene material
CN104166198B (en) * 2012-12-13 2018-06-12 苏州亨利通信材料有限公司 The manufacturing process of high intensity foaming packing gasket
CN103113653B (en) * 2013-02-06 2015-05-13 常州大学 HDPE (high-density polyethylene)/LDPE (low-density polyethylene) blended foam material and preparation method thereof
CN103113653A (en) * 2013-02-06 2013-05-22 常州大学 HDPE (high-density polyethylene)/LDPE (low-density polyethylene) blended foam material and preparation method thereof
CN105551585A (en) * 2015-12-16 2016-05-04 江苏亨通线缆科技有限公司 High-strength high-fire-retardance locomotive cable
CN105551585B (en) * 2015-12-16 2018-01-09 江苏亨通线缆科技有限公司 High-intensity high combustion locomotive cable
CN105469867B (en) * 2015-12-16 2018-04-13 江苏亨通线缆科技有限公司 Wear-resistant special cable used for rolling stock
CN105469867A (en) * 2015-12-16 2016-04-06 江苏亨通线缆科技有限公司 Special cable for wear-resistant locomotive vehicle

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