CN102942711A - Processing technique for rubber - Google Patents

Processing technique for rubber Download PDF

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Publication number
CN102942711A
CN102942711A CN2012104470030A CN201210447003A CN102942711A CN 102942711 A CN102942711 A CN 102942711A CN 2012104470030 A CN2012104470030 A CN 2012104470030A CN 201210447003 A CN201210447003 A CN 201210447003A CN 102942711 A CN102942711 A CN 102942711A
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CN
China
Prior art keywords
rubber
massfraction
refining
desulfurization
complete processing
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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
Application number
CN2012104470030A
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Chinese (zh)
Inventor
郭夕军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JIANGSU DONGXU TECHNOLOGY Co Ltd
Original Assignee
JIANGSU DONGXU TECHNOLOGY Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by JIANGSU DONGXU TECHNOLOGY Co Ltd filed Critical JIANGSU DONGXU TECHNOLOGY Co Ltd
Priority to CN2012104470030A priority Critical patent/CN102942711A/en
Publication of CN102942711A publication Critical patent/CN102942711A/en
Pending legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

The invention discloses a processing technique for rubber. The processing technique comprises the following steps of: extracting 10-30 percent of natural rubber, 15-20 percent of butadiene styrene rubber, 40-55 percent of regenerated rubber, 10-15 percent of softening agent, 8-10 percent of activating agent and 0.4-0.6 percent of assistant, in terms of mass fraction; mixing the components; desulfurizing the mixture at high temperature and high pressure; and roughly smelting and refining the desulfurized mixture to obtain a finished product. The processing technique disclosed by the invention has the advantages that the processing flow of the rubber is simple and convenient; and the produced products are high in quality and strong in wear resistance.

Description

A kind of complete processing of rubber
Technical field
The present invention relates to rubber process, relate in particular to a kind of complete processing of rubber.
Background technology
Under the competition comparison rugged environment of current social since rubber be a kind of recyclable recycling resource, and second development and utilization need to its by every treatment process just can reach effect that new product can reach like this certainly will so that the difficulty of this technique greatly promote, but complete processing how to study a kind of recycled rubber for enterprise has determined the competitive power of the product of enterprise.
Summary of the invention
The complete processing that the purpose of this invention is to provide a kind of rubber.
The technical solution used in the present invention is:
A kind of complete processing of rubber, the natural rubber, the styrene-butadiene rubber(SBR) of 15-20 massfraction, the regenerated rubber of 40-55 massfraction, the tenderizer of 10-15 massfraction, the activator of 8-10 massfraction and the auxiliary agent of 0.4-0.6 massfraction that extract the 10-30 massfraction mix, carry out high temperature, high pressure desulfurization, then slightly refining, refining forms again.
The massfraction of described natural rubber is 12-25, the massfraction of described styrene-butadiene rubber(SBR) is 16-18, and the massfraction of described regenerated rubber is 42-53, and the massfraction of described tenderizer is 11-13, the massfraction of described activator is 9-10, and the massfraction of described auxiliary agent is 0.45-0.58.
The temperature of described refining is 100 ℃-130 ℃, and the time of described refining is 40-60 minute.
In the step of described high temperature, high pressure desulfurization, its desulfurization temperature is 220 ℃-265 ℃, and described pressure is 2.9-3.2MPA, and described desulfurization time is 45-60 minute.
Described tenderizer is one or both combinations in Stockholm tar, rosin, Yatall MA and the wood pitch, described activator is a kind of in sulfurous gas, lead nitrate, yellow soda ash, sodium hydroxide and the lead salt, and described auxiliary agent is a kind of among paracril, grafted CR adhesive, SBS, SIS, the SEBS.
Advantage of the present invention is: the work flow of this rubber is simple and convenient, and good product quality and the fastness to rubbing produced are strong.
Embodiment
Embodiment 1
A kind of complete processing of rubber, extracting the natural rubber of 10 massfractions, the styrene-butadiene rubber(SBR) of 15 massfractions, the regenerated rubber of 40 massfractions, the tenderizer of 10 massfractions, the activator of 9 massfractions and the auxiliary agent of 0.5 massfraction mixes, carry out high temperature, high pressure desulfurization, then slightly refining, refining forms again.
The temperature of described refining is 120 ℃, and the time of described refining is 45 minutes.
In the step of described high temperature, high pressure desulfurization, its desulfurization temperature is 250 ℃, and described pressure is 2.9MPA, and described desulfurization time is 45 minutes.
Described tenderizer is the mixing of Stockholm tar and rosin, and described activator is sulfurous gas, and described auxiliary agent is paracril.
Embodiment 2
A kind of complete processing of rubber, extracting the natural rubber of 30 massfractions, the styrene-butadiene rubber(SBR) of 20 massfractions, the regenerated rubber of 55 massfractions, the tenderizer of 15 massfractions, the activator of 10 massfractions and the auxiliary agent of 0.58 massfraction mixes, carry out high temperature, high pressure desulfurization, then slightly refining, refining forms again.
The temperature of described refining is 130 ℃, and the time of described refining is 60 minutes.
In the step of described high temperature, high pressure desulfurization, its desulfurization temperature is 265 ℃, and described pressure is 3.2MPA, and described desulfurization time is 60 minutes.
Described tenderizer is the mixing of Yatall MA and wood pitch, and described activator is lead nitrate, and described auxiliary agent is grafted CR adhesive.
Embodiment 3
A kind of complete processing of rubber, extracting the natural rubber of 25 massfractions, the styrene-butadiene rubber(SBR) of 18 massfractions, the regenerated rubber of 47 massfractions, the tenderizer of 13 massfractions, the activator of 9 massfractions and the auxiliary agent of 0.55 massfraction mixes, carry out high temperature, high pressure desulfurization, then slightly refining, refining forms again.
The temperature of described refining is 100 ℃, and the time of described refining is 50 minutes.
In the step of described high temperature, high pressure desulfurization, its desulfurization temperature is 240 ℃, and described pressure is 3.1MPA, and described desulfurization time is 50 minutes.
Described tenderizer is the mixing of Stockholm tar and wood pitch, and described activator is sodium hydroxide, and described auxiliary agent is SEBS.

Claims (5)

1. the complete processing of a rubber, it is characterized in that: the natural rubber, the styrene-butadiene rubber(SBR) of 15-20 massfraction, the regenerated rubber of 40-55 massfraction, the tenderizer of 10-15 massfraction, the activator of 8-10 massfraction and the auxiliary agent of 0.4-0.6 massfraction that extract the 10-30 massfraction mix, carry out high temperature, high pressure desulfurization, then slightly refining, refining forms again.
2. the complete processing of a kind of rubber according to claim 1, it is characterized in that: the massfraction of described natural rubber is 12-25, the massfraction of described styrene-butadiene rubber(SBR) is 16-18, the massfraction of described regenerated rubber is 42-53, the massfraction of described tenderizer is 11-13, the massfraction of described activator is 9-10, and the massfraction of described auxiliary agent is 0.45-0.58.
3. the complete processing of a kind of rubber according to claim 1, it is characterized in that: the temperature of described refining is 100 ℃-130 ℃, and the time of described refining is 40-60 minute.
4. the complete processing of a kind of rubber according to claim 1, it is characterized in that: in the step of described high temperature, high pressure desulfurization, its desulfurization temperature is 220 ℃-265 ℃, and described pressure is 2.9-3.2MPA, and described desulfurization time is 45-60 minute.
5. the complete processing of a kind of rubber according to claim 1, it is characterized in that: described tenderizer is one or both combinations in Stockholm tar, rosin, Yatall MA and the wood pitch, described activator is a kind of in sulfurous gas, lead nitrate, yellow soda ash, sodium hydroxide and the lead salt, and described auxiliary agent is a kind of among paracril, grafted CR adhesive, SBS, SIS, the SEBS.
CN2012104470030A 2012-11-12 2012-11-12 Processing technique for rubber Pending CN102942711A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012104470030A CN102942711A (en) 2012-11-12 2012-11-12 Processing technique for rubber

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Application Number Priority Date Filing Date Title
CN2012104470030A CN102942711A (en) 2012-11-12 2012-11-12 Processing technique for rubber

Publications (1)

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CN102942711A true CN102942711A (en) 2013-02-27

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103319756A (en) * 2013-06-03 2013-09-25 宁波千汇汽车饰件有限公司 Preparation technology of engine rubber pad
CN103756074A (en) * 2013-12-25 2014-04-30 山东恒宇科技有限公司 Machining process of rubber
CN104861243A (en) * 2015-05-06 2015-08-26 吴芳吉 Engine rubber cushion block production technology
CN104861223A (en) * 2015-05-06 2015-08-26 吴芳吉 Car rubber cushion block
CN104877207A (en) * 2015-05-06 2015-09-02 吴芳吉 Preparation process for rubber cushion block of numerical control milling machine
CN108586839A (en) * 2018-05-10 2018-09-28 来安县隆华摩擦材料有限公司 A kind of production technology of Friction Facing on Clutch Disc in Heavy production rubber mass
CN109422943A (en) * 2017-08-28 2019-03-05 中国石油化工股份有限公司 It is a kind of for exempting to inflate the raw material of rickshaw tire and exempting to inflate rickshaw tire and preparation method thereof
CN109503913A (en) * 2017-09-14 2019-03-22 中国石油化工股份有限公司 One kind is exempted to inflate fretting map rickshaw tire raw material and exempts to inflate fretting map rickshaw tire and preparation method thereof
CN109852078A (en) * 2018-11-20 2019-06-07 苏州卓宝科技有限公司 A kind of environment protection modified pitch and its processing method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1666999A (en) * 2005-02-21 2005-09-14 株洲时代新材料科技股份有限公司 Process for preparing in-situ graft modified rubber by using general rubber preparing device and its modifier
CN101747543A (en) * 2009-12-09 2010-06-23 浙江仕峰实业有限公司 Styrene-butadiene copolymer chemical foaming composition containing polystyrene micro-blocks, preparation method and application method thereof

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1666999A (en) * 2005-02-21 2005-09-14 株洲时代新材料科技股份有限公司 Process for preparing in-situ graft modified rubber by using general rubber preparing device and its modifier
CN101747543A (en) * 2009-12-09 2010-06-23 浙江仕峰实业有限公司 Styrene-butadiene copolymer chemical foaming composition containing polystyrene micro-blocks, preparation method and application method thereof

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103319756A (en) * 2013-06-03 2013-09-25 宁波千汇汽车饰件有限公司 Preparation technology of engine rubber pad
CN103319756B (en) * 2013-06-03 2015-08-26 宁波千汇汽车饰件有限公司 A kind of preparation technology of engine rubber pad
CN103756074A (en) * 2013-12-25 2014-04-30 山东恒宇科技有限公司 Machining process of rubber
CN104861243A (en) * 2015-05-06 2015-08-26 吴芳吉 Engine rubber cushion block production technology
CN104861223A (en) * 2015-05-06 2015-08-26 吴芳吉 Car rubber cushion block
CN104877207A (en) * 2015-05-06 2015-09-02 吴芳吉 Preparation process for rubber cushion block of numerical control milling machine
CN109422943A (en) * 2017-08-28 2019-03-05 中国石油化工股份有限公司 It is a kind of for exempting to inflate the raw material of rickshaw tire and exempting to inflate rickshaw tire and preparation method thereof
CN109503913A (en) * 2017-09-14 2019-03-22 中国石油化工股份有限公司 One kind is exempted to inflate fretting map rickshaw tire raw material and exempts to inflate fretting map rickshaw tire and preparation method thereof
CN108586839A (en) * 2018-05-10 2018-09-28 来安县隆华摩擦材料有限公司 A kind of production technology of Friction Facing on Clutch Disc in Heavy production rubber mass
CN109852078A (en) * 2018-11-20 2019-06-07 苏州卓宝科技有限公司 A kind of environment protection modified pitch and its processing method

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Application publication date: 20130227