Preparation of polymer modified bitumen (PMB) from polyethylene terephthalate (PET) derived polyamido amine

US9528001B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9528001-B2
Application numberUS-201514659089-A
CountryUS
Kind codeB2
Filing dateMar 16, 2015
Priority dateMar 26, 2014
Publication dateDec 27, 2016
Grant dateDec 27, 2016

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

Official abstract text for this publication.

The present invention relates a novel approach to prepare Polymer Modified Bitumen by using terephthalamide additives, derived from PET, for improving bitumen quality. Particularly, the present invention provides a process to utilize waste PET, which is a threat to environment and is available commercially in different physical forms, for conversion into industrially useful additive for bituminous product.

First claim

Opening claim text (preview).

We claim: 1. A process for preparing modified bitumen, the process comprising of: (i) reacting polyethylene terephthalate (PET) with amines or polyamines to obtain amido amines or polyamido amines; (ii) reacting the amido amines or polyamido amines as obtained in step (i) with isocyanate or polyisocyanate and bitumen in a solvent to obtain modified bitumen. 2. The process as claimed in claim 1 , wherein amido amines or polyamido amines are reacted with isocyanate or polyisocyanate, prior to reacting with bitumen. 3. The process as claimed in claim 1 , wherein amido amines or polyamido amines; isocyanate or polyisocyanate; and bitumen are reacted simultaneously. 4. The process as claimed in claim 1 , wherein amido amines, or polyamido amines are present in 0.05-30% wt/wt of bitumen. 5. The process as claimed in claim 1 , wherein the isocyanates or polyisocyanates are present in 0.05-30% wt/wt of bitumen. 6. The process as claimed in claim 1 , wherein the reaction is conducted at a temperature of 50° C. to 190° C. 7. The process as claimed in claim 1 , wherein the reaction is conducted for a period of 10 minutes to 8 hours. 8. The process as claimed in claim 1 , wherein amines or polyamines are selected from the group comprising ethylene diamine, triethylene tetramine, propylene diamine, trimethylene diamine, hexamethylene diamine, decamethylene diamine, octamethylene diamine, di(heptamethylene)triamine, tripropylene tetramine, tetraethylene pentamine, trimethylene diamine, pentaethylene hexamine, di(trimethylene)triamine, N-(2-aminoethyl)piperazine, 1,4-bis(2-aminoethyl)piperazine, an aromatic polyamine selected from phenylene and napthylene diamines or hydrazines such as hydrazine, organo-hydrazines having hydrocarbon-based substituents of up to about 30 carbon atoms. 9. The process as claimed in claim 1 , wherein isocyantes or polyisocyanates are selected from the group comprising hexamethylene diisocyanate (HDI), trimethyl hexamethylene diisocyanate (HMDI), ethylene diisocyanate, ethylidene diisocyanate, propylene, butylene diisocyanate, diisocyanate dichlorohexaméthylène, furfurylidene diisocyanate, cycloaliphatic polyisocyanates, like isophorone diisocyanate (IPDI), cyclopentylene-1,3-diisocyanate, cyclohexylenedimethylene-1-diisocyanate, cyclohexylene-1,2-diisocyanate, and mixtures thereof, aromatic polyisocyanates like the 4,4′-diphenyl diisocyanate (MDI) and its isomers, such as 2,4′- and 2,2′-diphenylmethane diisocyanate, toluene diisocyanate (TDI) and isomers thereof, particularly the 2,4- and 2,6-toluene diisocyanate, 2,2-diphenylpropane-4′-diisocyanate, p-phenylene diisocyanate, m-phenylene diisocyanate, xylene diisocyanate, 1,4-naphthalene diisocyanate, 1,5-naphthalene diisocyanate, azobenzene-4,4′-diisocyanate, diphenyl sulfone-4,4′-diisocyanate, 1-chlorobenzene-2,4-diisocyanate, 4,4′,4″-triisocyanatotripheriyl methane, 1,3,5-triisocyanato-tetraisocyanate, and mixtures thereof. 10. The process as claimed in claim 1 , wherein the solvent is selected from dimethyl formamide (DMF), dimethyl sulphoxide (DMSO), acetone, methylethyl ketone, tetrahydrofuran (THF), ethyl acetate, benzene, toluene, chlorobenzene, hexane, cylohexane, xylene and dichloro methane (DCM). 11. The process as claimed in claim 1 , wherein the polyisocyante is diisocyanates, selected from MDI and its isomers, TDI and its isomers, HDI, IPDI and derivatives thereof. 12. The process as claimed in claim 1 , wherein amido amines or polyamido amines and isocyanate or polyisocyanate are reacted to obtain a polyurea. 13. A bituminous cement mixture comprising polyurethane or polyurea polymers as claimed in claim 12 , in body of bitumen. 14. A bituminous concrete comprising bituminous cement mixture of claim 1 and an aggregate.

Assignees

Inventors

Classifications

  • Polyureas · CPC title

  • from compounds containing nitrogen and active hydrogen, the nitrogen atom not being part of an isocyanate group · CPC title

  • Polyamides · CPC title

  • Polyamidoamines · CPC title

  • Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers · CPC title

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What does patent US9528001B2 cover?
The present invention relates a novel approach to prepare Polymer Modified Bitumen by using terephthalamide additives, derived from PET, for improving bitumen quality. Particularly, the present invention provides a process to utilize waste PET, which is a threat to environment and is available commercially in different physical forms, for conversion into industrially useful additive for bitumin…
Who is the assignee on this patent?
Indian Oil Corp Ltd
What technology area does this patent fall under?
Primary CPC classification C08L95/00. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Dec 27 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).