CN1347960A - Technological process of producing modified asphalt with waste polymer - Google Patents

Technological process of producing modified asphalt with waste polymer Download PDF

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Publication number
CN1347960A
CN1347960A CN 01135978 CN01135978A CN1347960A CN 1347960 A CN1347960 A CN 1347960A CN 01135978 CN01135978 CN 01135978 CN 01135978 A CN01135978 A CN 01135978A CN 1347960 A CN1347960 A CN 1347960A
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CN
China
Prior art keywords
rubber
waste polymer
plastics
waste
modified asphalt
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Granted
Application number
CN 01135978
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Chinese (zh)
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CN1137958C (en
Inventor
田富才
石应四
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Individual
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Individual
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Priority to CNB011359781A priority Critical patent/CN1137958C/en
Publication of CN1347960A publication Critical patent/CN1347960A/en
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Publication of CN1137958C publication Critical patent/CN1137958C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

The technological process of producing modified asphalt with waste polymer includes the following steps: cleaning and sorting to eliminate inorganic impurities in waste polymer and sort plastic and rubber; pelletization to produce 20 mm over below size plastic grains in a extruder and a pelletizer and to pulverize rubber in a pulverizer into 2 mm over below size rubber grains; producing paste to mix the pelletized polymer in 1-3 portions and residual oil in 10 portions and smelting the mixture in a container at 220-320 deg.c; and oxidation with blown in air at 220-255 deg.c up to a penetration degree of 30-200. The present invention is superior to available technology in that it produces modified asphalt in greatly lowered cost with waste.

Description

Use technological process of producing modified asphalt with waste polymer
Technical field:
The present invention relates to a kind of technology of producing modifying asphalt with waste polymer.
Background technology:
Traditional pitch is produced through oxidation by the residual oil of refinery, and its physical properties temperature influence is very big, and the crisp summer in winter is soft, its use is very restricted, and present modifying asphalt carries out modification owing to be subjected to raw-material restriction as adopting SBS styrene-butadiene rubber(SBR), and cost is higher, only be applied to some special occasions, be difficult to big area and promote, and present waste polymer is all abandoning as rubbish under the situation mostly as carving old tire etc., not only pollute environment, also caused the waste of resource.
Technology contents:
The purpose of this invention is to provide and a kind ofly produce the processing method of modifying asphalt, the cost of producing modifying asphalt is reduced greatly, and can solve present waste polymer and abandon the problem of environmental pollution that is produced everywhere with waste polymer.
Processing method of the present invention comprises following process:
Clean classification: the inorganic impurity in the waste polymer is removed totally, kept plastics and rubber and be divided into two classes by plastics and rubber;
Granulation: above-mentioned plastics class is inserted extruding machine make strip or make particulate state with tablets press, diameter or particle diameter are less than or equal to 20mm, and rubber-like then is crushed to the particulate state that is less than or equal to 2mm with pulverizer;
Glue: get 10 parts of residual oil and mix with waste polymer after 1~3 part of above-mentioned granulation, in the container under 220~320 ℃ of temperature fully fusing mix thoroughly;
Oxidation: under 220~255 ℃ of temperature condition, be blown into air, reach 30~200 to penetration degree and promptly make modifying asphalt of the present invention.
Compared with prior art, the present invention reduces the cost of producing modifying asphalt greatly, and can solve the pollution problem of present waste polymer, turns waste into wealth.
Embodiment:
Embodiment 1:
Waste polymer inserted in the service sink wash, dry moisture after removing inorganic impurity wherein, sort out plastics and rubber two classes, above-mentioned plastics class is inserted extruding machine make strip below the diameter 20mm, rubber-like then is crushed to particulate state below the 2mm with pulverizer, get 10 parts of residual oil and mix with waste polymer after 1 part of above-mentioned granulation, in the container under 250 ℃ of temperature fully fusing mix thoroughly; Under 230 ℃ of temperature condition, be blown into air, reach 40 to penetration degree and promptly make modifying asphalt of the present invention.
Embodiment 2:
Inorganic impurity in the waste polymer is removed, sort out plastics and rubber two classes, above-mentioned plastics class is inserted tablets press make the following particulate state of 20mm, rubber-like then is crushed to particulate state below the 2mm with pulverizer, get 10 parts of residual oil and mix with waste polymer after 3 parts of above-mentioned granulations, in the container under 300 ℃ of temperature fully fusing mix thoroughly; Under 250 ℃ of temperature condition, be blown into air, reach 70 to penetration degree and promptly make modifying asphalt of the present invention.
Embodiment 3:
Inorganic impurity in the waste polymer is removed, sort out plastics and rubber two classes, above-mentioned plastics class is inserted tablets press make the following particulate state of 15mm, rubber-like then is crushed to particulate state below the 2mm with pulverizer, get 10 parts of residual oil and mix with waste polymer after 2 parts of above-mentioned granulations, in the container under 280 ℃ of temperature fully fusing mix thoroughly; Under 255 ℃ of temperature condition, be blown into air, reach 200 to penetration degree and promptly make modifying asphalt of the present invention.
Embodiment 2:
Inorganic impurity in the waste polymer is removed, sort out plastics and rubber two classes, above-mentioned plastics class is inserted tablets press make the following particulate state of 10mm, rubber-like then is crushed to particulate state below the 2mm with pulverizer, get 10 parts of residual oil and mix with waste polymer after 2.5 parts of above-mentioned granulations, in the container under 320 ℃ of temperature fully fusing mix thoroughly; Under 220 ℃ of temperature condition, be blown into air, reach 150 to penetration degree and promptly make modifying asphalt of the present invention.

Claims (2)

1, a kind of technological process of producing modified asphalt with waste polymer of using is characterized in that comprising following process:
Clean classification: the inorganic impurity in the waste polymer is removed totally, kept plastics and rubber and be divided into two classes by plastics and rubber;
Granulation: above-mentioned plastics class is inserted extruding machine make strip, diameter is less than or equal to 20mm, and rubber-like then is crushed to the particulate state that is less than or equal to 2mm with pulverizer;
Glue: get 10 parts of residual oil and mix with waste polymer after 1~3 part of above-mentioned granulation, in the container under 220~320 ℃ of temperature fully fusing mix thoroughly;
Oxidation: under 220~255 ℃ of temperature condition, be blown into air, reach 30~200 to penetration degree and promptly make modifying asphalt of the present invention.
2, a kind of technological process of producing modified asphalt with waste polymer of using is characterized in that comprising following process:
Clean classification: the inorganic impurity in the waste polymer is removed totally, kept plastics and rubber and be divided into two classes by plastics and rubber;
Granulation: above-mentioned plastics class is inserted tablets press make particulate state, particle diameter is less than or equal to 20mm, and rubber-like then is crushed to the particulate state that is less than or equal to 2mm with pulverizer;
Glue: get 10 parts of residual oil and mix with waste polymer after 1~3 part of above-mentioned granulation, in the container under 220~320 ℃ of temperature fully fusing mix thoroughly;
Oxidation: under 220~255 ℃ of temperature condition, be blown into air, reach 30~200 to penetration degree and promptly make modifying asphalt of the present invention.
CNB011359781A 2001-10-26 2001-10-26 Technological process of producing modified asphalt with waste polymer Expired - Fee Related CN1137958C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB011359781A CN1137958C (en) 2001-10-26 2001-10-26 Technological process of producing modified asphalt with waste polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB011359781A CN1137958C (en) 2001-10-26 2001-10-26 Technological process of producing modified asphalt with waste polymer

Publications (2)

Publication Number Publication Date
CN1347960A true CN1347960A (en) 2002-05-08
CN1137958C CN1137958C (en) 2004-02-11

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Family Applications (1)

Application Number Title Priority Date Filing Date
CNB011359781A Expired - Fee Related CN1137958C (en) 2001-10-26 2001-10-26 Technological process of producing modified asphalt with waste polymer

Country Status (1)

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CN (1) CN1137958C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100410327C (en) * 2005-03-14 2008-08-13 天津鑫业工贸发展有限公司 Process for preparing waste-tyre rubber-powder modified pitch, and its host machine
CN101054451B (en) * 2007-05-22 2010-05-26 杨林江 Artificial asphalt for pavement and preparation method thereof
CN103992808A (en) * 2014-05-21 2014-08-20 常熟市联邦化工有限公司 Process for recycling C10 heavy aromatic residue oil

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101225237B (en) * 2008-01-25 2010-07-14 杨锡武 Method for preparing modified asphalt by using waste plastics

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100410327C (en) * 2005-03-14 2008-08-13 天津鑫业工贸发展有限公司 Process for preparing waste-tyre rubber-powder modified pitch, and its host machine
CN101054451B (en) * 2007-05-22 2010-05-26 杨林江 Artificial asphalt for pavement and preparation method thereof
CN103992808A (en) * 2014-05-21 2014-08-20 常熟市联邦化工有限公司 Process for recycling C10 heavy aromatic residue oil

Also Published As

Publication number Publication date
CN1137958C (en) 2004-02-11

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Granted publication date: 20040211

Termination date: 20131026