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CN111286128A - Quickly-molded polybutylene resin and preparation method thereof - Google Patents

Quickly-molded polybutylene resin and preparation method thereof Download PDF

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Publication number
CN111286128A
CN111286128A CN202010223348.2A CN202010223348A CN111286128A CN 111286128 A CN111286128 A CN 111286128A CN 202010223348 A CN202010223348 A CN 202010223348A CN 111286128 A CN111286128 A CN 111286128A
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parts
polybutene
resin
antioxidant
filler
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CN111286128B (en
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刘晨光
贺爱华
邵华锋
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Qingdao University of Science and Technology
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Qingdao University of Science and Technology
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/18Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
    • C08L23/20Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K2003/2237Oxides; Hydroxides of metals of titanium
    • C08K2003/2241Titanium dioxide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • C08K2003/265Calcium, strontium or barium carbonate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/08Stabilised against heat, light or radiation or oxydation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/24Crystallisation aids

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

The invention relates to a quickly-formed polybutylene resin and a preparation method thereof, belonging to the field of high polymer materials. The components of the color masterbatch comprise polybutylene, an antioxidant, a halogen absorbing agent, a light stabilizer, a color masterbatch, a nucleating agent and a filler; the preparation method comprises the steps of uniformly mixing the polybutene, the antioxidant, the halogen absorbing agent, the light stabilizer, the color master batch, the nucleating agent and the filler by a high-speed stirring mixer, and carrying out melt extrusion granulation to obtain the polybutene resin. The resin has the characteristics of high crystal form transformation speed, high heat-resistant temperature and the like, and can be used as a cold and hot water pipe material.

Description

Quickly-molded polybutylene resin and preparation method thereof
Technical Field
The invention relates to a polybutylene resin with rapid crystal form transformation and high thermal deformation temperature, a preparation method and application thereof, belonging to the field of high polymer materials, in particular to the processing and application of the high polymer materials.
Background
The high Isotactic Polybutene (iPB) has outstanding hot creep resistance, environmental stress cracking resistance, high heat resistance temperature and good toughness, and is one of the best materials for the pipe and the connecting piece thereof.
Different from other pipes, the polybutene is melt processed to directly form a metastable crystal form II, and the crystal form II is gradually converted into a stable crystal form I at room temperature. The crystal form of the polybutene is slowly transformed, the transformation time is long (more than 7 days), and in the process of transforming the crystal form, the size of the product is reduced and the strength is increased. Therefore, the polybutene can be transported and applied after being placed at room temperature for more than one week until the crystal form transformation is completed, so that the molding time of the polybutene product is greatly prolonged, and the turnover period of the product is remarkably prolonged. Therefore, the development of a polybutene material with rapid forming (rapid crystal transformation) is of great significance.
CN105273320A discloses a method for adding graphene into polybutene, which accelerates the II-I crystal form transformation of polybutene and improves the mechanical properties of polybutene, but the expensive graphene makes the product have higher cost. The Chinese patent ZL200410032739.7 discloses that acetylene black is used as a nucleating agent to promote the crystal transformation of a 1-butene homopolymer or a 1-butene copolymer and improve the chlorine water resistance of the copolymer. CN104629195B discloses that polybutene in-kettle alloys containing a polypropylene component are prepared by in-kettle polymerization technology, and the crystal form transformation rate can be accelerated. Japanese patent 2618469 discloses that adding propylene homopolymer and HDPE to polybutene shortens the crystal transition period, but the addition of propylene homopolymer and HDPE deteriorates some of its properties.
CN101020777B discloses that a high-thermal-conductivity polybutylene coil pipe is prepared by adding graphite with surface treatment, the pressure resistance and the heat resistance of a product are improved, but the problems of crystal form transformation and rapid forming of polybutylene are not involved. CN105504552B, CN105754233A, and CN1016151774A disclose reinforced polybutylene pipeline material and preparation method thereof, but none of the above patents relate to the problem of rapid molding of polybutylene.
Disclosure of Invention
One of the purposes of the invention is to solve the problem that the crystal form of the polybutene is slowly changed (more than one week), and provide a formula of the polybutene resin for quick forming.
The invention also aims to further improve the heat deformation temperature of the polybutylene resin and improve the heat resistance of the polybutylene resin.
The invention also aims to provide a preparation method of the quick-forming polybutylene resin.
A quickly-formed polybutylene resin comprises the following components in parts by weight:
polybutene 100 parts
0.1-5 parts of antioxidant
0.01-2 parts of halogen absorbing agent
0.01-2 parts of light stabilizer
0.1-5 parts of color masterbatch
0.01-5 parts of nucleating agent
0.1 to 10 portions of filler
The isotactic degree of polybutene in the polybutene resin is more than 96 wt.%, and the melt mass flow rate is 0.2-3g/10min (190 ℃, 2.16 kg). The antioxidant comprises a main antioxidant and an auxiliary antioxidant, the weight ratio of the main antioxidant to the auxiliary antioxidant is 1: 0.5-4, wherein the main antioxidant is selected from one or more of BHT, Hostanox3, 3114, 1010 and 1076, and the auxiliary antioxidant is selected from one or more of 168, 626, 9228, DLTDP, DSTP, DMTDP and DTDTDTP.
The halogen absorbing agent is one or more of hydrotalcite, calcium stearate, sodium stearate or zinc stearate.
The light stabilizer is one or more of benzophenones or hindered amines.
The nucleating agent is one or a mixture of two or more of 3, 4-dimethyl benzyl sorbitol, bicyclo [2, 2, 1] disodium heptanedionate, sodium bis (p-tert-butylphenyl) phosphate, aromatic amide compounds and derivatives thereof.
The color master batch comprises the following components in parts by weight: 40-95 parts of high isotactic polybutene (isotacticity greater than 96 wt.%); 0.1-6 parts of polyethylene wax or polypropylene wax; 0.1-6 parts of titanium dioxide; 0.001-6 parts of pigment; 0.01-3 parts of an anti-aging agent.
The filler is one or more of calcium carbonate, talcum powder, mica and kaolin.
A preparation method of quickly molded polybutylene resin comprises the following specific preparation steps:
(1) all the raw materials (polybutene, antioxidant, halogen absorbing agent, light stabilizer, color masterbatch, nucleating agent and filler) weighed according to the proportion are uniformly mixed in a high-speed stirring mixer;
(2) adding the uniformly mixed materials in the step (1) into a double-screw extruder with the length-diameter ratio of 30-50: 1, and performing melt extrusion, wherein the extrusion process comprises the following steps: the first zone is 150-.
(3) And (3) granulating and drying the extrudate obtained in the step (2) to obtain the polybutene resin.
The polybutene resin prepared by the invention maintains the excellent shock resistance, excellent heat creep resistance and outstanding environmental stress cracking resistance of polybutene, meanwhile, the crystal form transformation speed is obviously improved, the heat resistance is obviously improved, and the polybutene resin can be used as cold and hot water pipes and pipe fittings.
Detailed Description
The following examples are presented to better illustrate the invention and are not to be construed as limiting the claims of the invention.
The isotactic degree of polybutene in the polybutene alloy resin used was 98. wt%, and the melt flow rate (190 ℃ C., load 2.16kg) was 0.5g/10 min. Measuring the characteristic peak-peak high variation curve of the polybutene crystal form I by using an online infrared spectrum to obtain the t of crystal form conversion1/2And the appearance time of the crystal form I, and the Vicat softening point of the polybutene is measured by a Vicat thermomechanical instrument (GB/T1633-2000A 50 method).
Comparative example 1
Weighing the materials according to the components and the formula (in parts by weight) provided in the table 1, wherein the main antioxidant is 1010 and the auxiliary antioxidant is 168, mixing the materials in a high-speed mixer for 5 minutes, and then extruding and granulating the mixture in a double-screw extruder with the length-diameter ratio of 45 and the diameter of 50 millimeters to obtain the polybutene material. The temperature of each section of the extruder is as follows: 150 ℃ in the first zone, 160 ℃ in the second zone, 170 ℃ in the third zone, 180 ℃ in the fourth zone, 190 ℃ in the fifth zone, 180 ℃ at the head, 20 revolutions per minute at the speed of the extruder and 15MPa of melt pressure.
The results of the performance tests are shown in Table 1.
Example 1
The materials were weighed according to the components and formulations (in parts by weight, the same in the following examples) provided in table 1, wherein the filler was calcium carbonate, the nucleating agent was 3, 4-dimethyldibenzyl sorbitol (nucleating agent 1), the primary antioxidant was 1010, the secondary antioxidant was 168, the halogen absorbing agent was calcium stearate, and the light stabilizer was benzophenone grease. The color master batch (color master 1) comprises the following components in parts by weight: 90 parts of high isotactic polybutene (98 wt.% of isotacticity), 3 parts of polypropylene wax, 3 parts of titanium dioxide, 0.01 part of pigment and 0.03 part of anti-aging agent.
After mixing for 5 minutes in a high-speed stirrer, extruding and granulating in a double-screw extruder with the length-diameter ratio of 45 and the diameter of 50 millimeters to obtain the polybutene resin. The temperature of each section of the extruder is as follows: 150 ℃ in the first zone, 160 ℃ in the second zone, 170 ℃ in the third zone, 180 ℃ in the fourth zone, 190 ℃ in the fifth zone, 180 ℃ at the head, 20 revolutions per minute at the speed of the extruder and 15MPa of melt pressure.
The results of the performance tests are shown in Table 1.
Example 2
The materials are weighed according to the components and the formula (in parts by weight) provided in table 1, wherein the filler is calcium carbonate, the nucleating agent is 3, 4-dimethyl benzyl sorbitol (nucleating agent 1), the main antioxidant is 1010, the auxiliary antioxidant is 168, the halogen absorbing agent is calcium stearate, and the light stabilizer is benzophenone grease. The color master batch (color master 1) comprises the following components in parts by weight: 90 parts of high isotactic polybutene (98 wt.% of isotacticity), 3 parts of polypropylene wax, 3 parts of titanium dioxide, 0.01 part of pigment and 0.03 part of anti-aging agent.
The rest is the same as example 1. The results of the performance tests are shown in Table 1.
Example 3
The materials are weighed according to the components and the formula (in parts by weight) provided in table 1, wherein the filler is calcium carbonate, the nucleating agent is 3, 4-dimethyl benzyl sorbitol (nucleating agent 1), the main antioxidant is 1010, the auxiliary antioxidant is 168, the halogen absorbing agent is calcium stearate, and the light stabilizer is benzophenone grease. The color master batch (color master 2) comprises the following components in parts by weight: 90 parts of high isotactic polybutene (98 wt.% of isotacticity), 1 part of polypropylene wax, 3 parts of titanium dioxide, 0.01 part of pigment and 0.03 part of anti-aging agent.
The rest is the same as example 1. The results of the performance tests are shown in Table 1.
Example 4
The materials were weighed according to the components and formulation (in parts by weight) provided in table 1, wherein the filler was calcium carbonate, the nucleating agent was an aromatic amide compound (nucleating agent 2), the primary antioxidant was 1010, the secondary antioxidant was 168, the halogen absorbing agent was calcium stearate, and the light stabilizer was benzophenone grease. The color master batch (color master 1) comprises the following components in parts by weight: 90 parts of high isotactic polybutene (98 wt.% of isotacticity), 3 parts of polypropylene wax, 3 parts of titanium dioxide, 0.01 part of pigment and 0.03 part of anti-aging agent.
The rest is the same as example 1. The results of the performance tests are shown in Table 1.
Example 5
The materials are weighed according to the components and the formula (in parts by weight) provided in table 1, wherein the filler is calcium carbonate, the nucleating agent is 3, 4-dimethyl benzyl sorbitol (nucleating agent 1), the main antioxidant is 1010, the auxiliary antioxidant is 168, the halogen absorbing agent is calcium stearate, and the light stabilizer is benzophenone grease. The color master batch (color master 1) comprises the following components in parts by weight: 90 parts of high isotactic polybutene (98 wt.% of isotacticity), 3 parts of polypropylene wax, 3 parts of titanium dioxide, 0.01 part of pigment and 0.03 part of anti-aging agent.
After mixing for 5 minutes in a high-speed stirrer, extruding and granulating in a double-screw extruder with the length-diameter ratio of 45 and the diameter of 50 millimeters to obtain the polybutene resin. The temperature of each section of the extruder is as follows: 155 ℃ in the first zone, 165 ℃ in the second zone, 175 ℃ in the third zone, 185 ℃ in the fourth zone, 195 ℃ in the fifth zone, 185 ℃ in the head, 25 revolutions per minute in the extruder and 15MPa in the melt pressure.
The results of the performance tests are shown in Table 1.
As can be seen from the results of the examples and comparative example 1, the crystal transformation speed of the polybutene resin of the present invention is greatly increased as compared with polybutene, and the heat resistance can be increased by 7.1 ℃.
TABLE 1 Components and formulations of the examples and comparative examples
Components Example 1 Example 2 Example 3 Example 4 Example 5 Comparative example 1
Polybutene/part by weight 100 100 100 100 100 100
Fillers/parts by weight 5 5 5 5 5 0
Nucleating agent 1/part by weight 0.3 0.5 0.3 0 0.3 0
Nucleating agent 2/part by weight 0 0 0 0.3 0 0
Main antioxidant per weight portion 0.1 0.1 0.1 0.1 0.1 0.1
Auxiliary antioxidant/part by weight 0.2 0.2 0.2 0.2 0.2 0.2
Halogen-absorbing agent/part by weight 0.1 0.1 0.1 0.1 0.1 0
Light stabilizer per part by weight 0.8 0.8 0.8 0.8 0.8 0
1 part by weight of color master batch 2 2 0 2 2 0
2 parts by weight of color master batch 0 0 2 0 0 0
T of crystal form transformation1/2Hour/hour 15.9 15.6 15.9 21.2 18.2 58.4
Time of appearance/hour of form I 3.0 2.8 3.0 4.1 3.6 19.7
Vicat softening point/. degree C 121.5 120.9 120.1 118.8 119.8 114.4

Claims (10)

1. A polybutylene resin for rapid prototyping is characterized by comprising the following components in parts by weight:
polybutene 100 parts
0.1-5 parts of antioxidant
0.01-2 parts of halogen absorbing agent
0.01-2 parts of light stabilizer
0.1-5 parts of color masterbatch
0.01-5 parts of nucleating agent
0.1-10 parts of filler.
2. A fast-forming polybutene resin as claimed in claim 1, wherein the polybutene in the polybutene resin has an isotacticity of more than 96 wt.%, a melt mass flow rate of 0.2-3g/10min at 2.16kg at 190 ℃.
3. The polybutylene resin with the rapid prototyping function according to any one of claims 1 or 2, wherein the antioxidant is composed of a main antioxidant and a secondary antioxidant, the weight ratio of the main antioxidant to the secondary antioxidant is 1: 0.5-4, wherein the main antioxidant is selected from one or more of BHT, Hostanox3, 3114, 1010 and 1076, and the secondary antioxidant is selected from one or more of 168, 626, 9228, DLTDP, DSTP, DMTDP and DTDTDTDTP.
4. A fast-forming polybutene resin as claimed in claim 1 or 2, wherein the halogen-absorbing agent is one or more of hydrotalcite, calcium stearate, sodium stearate or zinc stearate.
5. The polybutylene resin for rapid prototyping according to any of claims 1 or 2, wherein the light stabilizer is one or more of benzophenones and hindered amines.
6. The polybutene resin as claimed in claim 1 or 2, wherein the nucleating agent is one or a mixture of two or more of 3, 4-dimethyldibenzyl sorbitol, disodium bicyclo [2, 2, 1] heptanedionate, sodium bis (p-tert-butylphenyl) phosphate, aromatic amides and their derivatives.
7. A fast-forming polybutene resin as claimed in claims 1 or 2, wherein the masterbatch comprises the following components in parts by weight: 40-95 parts of high isotactic polybutene (isotacticity greater than 96 wt.%); 0.1-6 parts of polyethylene wax or polypropylene wax; 0.1-6 parts of titanium dioxide; 0.001-6 parts of pigment; 0.01-3 parts of an anti-aging agent.
8. A polybutene resin as claimed in claim 1 or 2, wherein the filler is one or more of calcium carbonate, talc, mica and kaolin.
9. A preparation method of quickly-formed polybutylene resin is characterized by comprising the following specific preparation steps:
(1) all the raw materials (polybutene, antioxidant, halogen absorbing agent, light stabilizer, color masterbatch, nucleating agent and filler) weighed according to the proportion are uniformly mixed in a high-speed stirring mixer;
(2) adding the uniformly mixed materials in the step (1) into a double-screw extruder with the length-diameter ratio of 30-50: 1, and performing melt extrusion, wherein the extrusion process comprises the following steps: the first zone is 150-;
(3) and (3) granulating and drying the extrudate obtained in the step (2) to obtain the polybutene resin.
10. The polybutene resin as claimed in claim 1 or 2, wherein the polybutene resin has a high transformation rate of crystal form and high heat-resistant temperature, and is used as a material for hot and cold water pipes.
CN202010223348.2A 2020-03-26 2020-03-26 Quickly-molded polybutylene resin and preparation method thereof Active CN111286128B (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113881151A (en) * 2020-07-02 2022-01-04 中国石油天然气股份有限公司 Special polybutylene resin composition for cold and hot water pipes and preparation method thereof
CN116144121A (en) * 2023-03-27 2023-05-23 青岛科技大学 Shape memory pipeline material with high heat creep resistance and preparation method thereof

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10237308A (en) * 1996-08-08 1998-09-08 New Japan Chem Co Ltd Rosin-based molecule crystal, nucleating agent for polyolefin resin, polyolefin resin composition and its molded product
CN1521203A (en) * 2002-06-24 2004-08-18 ��绯��ҵ��ʽ���� Nucleating agent and crystalline polymer composition containing the same
WO2005047383A1 (en) * 2003-11-07 2005-05-26 Milliken & Company Concentrates of saturated bicyclic dicarboxylate salts as polymer nucleation additives and methods of nucleating thermoplastics
JP2007186563A (en) * 2006-01-12 2007-07-26 Mitsui Chemicals Inc Polybutene resin composition
CN104194111A (en) * 2013-10-31 2014-12-10 中国石油化工股份有限公司 A polyolefin resin composition containing a nucleating agent and a preparing method thereof
CN104629195A (en) * 2015-02-15 2015-05-20 青岛科技大学 Special polybutylene alloy pipe material for cold/hot water pipe and preparation method of special polybutylene alloy pipe material
CN105504552A (en) * 2016-02-03 2016-04-20 山东东方宏业化工有限公司 Polybutylene material for pipes and preparation method of polybutylene material
CN106147044A (en) * 2016-07-07 2016-11-23 山西省化工研究所(有限公司) The compositions of a kind of isotactic polybutene 1 and binary acid diamide nucleator and preparation thereof
CN106147046A (en) * 2016-07-07 2016-11-23 山西省化工研究所(有限公司) The compositions of a kind of isotactic polybutene 1 and binary acid diamide nucleator and preparation thereof
CN110791028A (en) * 2019-11-11 2020-02-14 太原科技大学 Preparation method and application of special aid for efficiently inducing crystal form transformation of polybutene-1

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10237308A (en) * 1996-08-08 1998-09-08 New Japan Chem Co Ltd Rosin-based molecule crystal, nucleating agent for polyolefin resin, polyolefin resin composition and its molded product
CN1521203A (en) * 2002-06-24 2004-08-18 ��绯��ҵ��ʽ���� Nucleating agent and crystalline polymer composition containing the same
WO2005047383A1 (en) * 2003-11-07 2005-05-26 Milliken & Company Concentrates of saturated bicyclic dicarboxylate salts as polymer nucleation additives and methods of nucleating thermoplastics
JP2007186563A (en) * 2006-01-12 2007-07-26 Mitsui Chemicals Inc Polybutene resin composition
CN104194111A (en) * 2013-10-31 2014-12-10 中国石油化工股份有限公司 A polyolefin resin composition containing a nucleating agent and a preparing method thereof
CN104629195A (en) * 2015-02-15 2015-05-20 青岛科技大学 Special polybutylene alloy pipe material for cold/hot water pipe and preparation method of special polybutylene alloy pipe material
CN105504552A (en) * 2016-02-03 2016-04-20 山东东方宏业化工有限公司 Polybutylene material for pipes and preparation method of polybutylene material
CN106147044A (en) * 2016-07-07 2016-11-23 山西省化工研究所(有限公司) The compositions of a kind of isotactic polybutene 1 and binary acid diamide nucleator and preparation thereof
CN106147046A (en) * 2016-07-07 2016-11-23 山西省化工研究所(有限公司) The compositions of a kind of isotactic polybutene 1 and binary acid diamide nucleator and preparation thereof
CN110791028A (en) * 2019-11-11 2020-02-14 太原科技大学 Preparation method and application of special aid for efficiently inducing crystal form transformation of polybutene-1

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
赵永仙等: "全同含量对聚丁烯-1室温结晶性能的影响", 《高分子材料科学与工程》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113881151A (en) * 2020-07-02 2022-01-04 中国石油天然气股份有限公司 Special polybutylene resin composition for cold and hot water pipes and preparation method thereof
CN116144121A (en) * 2023-03-27 2023-05-23 青岛科技大学 Shape memory pipeline material with high heat creep resistance and preparation method thereof

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