Process for friction reduction during ethanol transport

US9822325B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9822325-B2
Application numberUS-201514713532-A
CountryUS
Kind codeB2
Filing dateMay 15, 2015
Priority dateMay 21, 2014
Publication dateNov 21, 2017
Grant dateNov 21, 2017

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

This invention involves a process for reducing friction in ethanol during its transport through pipelines. This process involves combining ethanol with a polymer-based composition, characterized in that the polymer is obtained from at least 50 mol % of at least one monomer selected from the group comprising N-substituted acrylamides, N-substituted methacrylamides, N,N-substituted acrylamides, N,N-substituted methacrylamides, substituted acrylates and substituted methacrylates.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for reducing friction during ethanol transport through pipelines, the process comprising combining ethanol with a polymer-based composition comprising a polymer obtained from at least 50 mol % of at least one non-ionic monomer selected from the group consisting of N-substituted acrylamides, N-substituted methacrylamides, N,N-substituted acrylamides, N,N-substituted methacrylamides, substituted acrylates and substituted methacrylates, wherein the quantity of polymer combined with ethanol ranges between 5 and 5,000 ppm in weight as regards the weight of ethanol. 2. The process according to claim 1 , wherein the polymer has a molecular weight ranging between 0.5 and 25 million g/mol. 3. The process according to claim 1 , wherein the at least one monomer has a substituted chain containing less than 30 carbon atoms. 4. The process according to claim 1 , wherein the N-substituted acrylamide monomers, N-substituted methacrylamide monomers, N,N-substituted acrylamide monomers and N,N-substituted methacrylamide monomers are selected from the group consisting of N-ethylacrylamide, N-isopropylacrylamide, N-tert-Butylacrylamide, Diacetoneacrylamide, N-hydroxyethylacrylamide, N-hydroxymethylacrylamide, N-alkyl acrylamide, N-[Tris(hydroxymethyl)methyl]acrylamide, N-acryloylmorpholine, N,N-Dimethylacrylamide, N,N-diethylacrylamide and N,N-dialkylacrylamide; alkyl representing an alkyl group comprising 3 to 22 carbon atoms. 5. The process according to claim 1 , wherein the substituted acrylate monomers and substituted methacrylate monomers are selected from the group consisting of methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, methyl methacrylate, ethyl methacrylate, propyl methacrylate, butyl methacrylate, other alkyl acrylate, alkyl methacrylate, isobornyl acrylate, isobornyl methacrylate, 2-ethylhexyl acrylate, 2-ethylhexyl methacrylate, Hydroxyethyl acrylate, Hydroxyethyl methacrylate, hydroxypropyl acrylate, hydroxypropyl methacrylate, furfuryl acrylate, furfuryl methacrylate, tetrahydrofurfuryl acrylate, tetrahydrofurfuryl methacrylate, glyceryl acrylate, glyceryl methacrylate, glycidyl acrylate, and glycidyle methacrylate; alkyl representing an alkyl group comprising 5 to 22 carbon atoms. 6. The process according to claim 1 , wherein the polymer additionally includes 5 mol % to less than 40 mol % of at least one ionic monomer. 7. The process according to claim 6 , wherein the ionic monomer is an anionic monomer selected from the group consisting of acrylic acid, methacrylic acid, itaconic acid, maleic acid, and 2-Acrylamido-2-methylpropane sulfonic acid (ATBS), the said anionic monomer being in its acid form, salified either partially or completely. 8. The process according to claim 1 , wherein the polymer includes at least 80 mol % of the at least one monomer selected from the group consisting of N-substituted acrylamides, N-substituted methacrylamides, N,N-substituted acrylamides, N,N-substituted methacrylamides, substituted acrylates and substituted methacrylates. 9. The process according to claim 1 , wherein the polymer is a polymer selected from the group consisting of N,N-dimethylacrylamide homopolymer, N,N-diethylacrylamide homopolymer, N,N-dimethylacrylamide copolymer and acrylic acid copolymer, N,N-diethylacrylamide copolymer and acrylic acid copolymer, N,N-dimethylacrylamide copolymer and 2-Acrylamido-2-methylpropane sulfonic acid copolymer and N,N-diethylacrylamide copolymer and 2-Acrylamido-2-methylpropane sulfonic acid copolymer. 10. The process according to claim 1 , wherein the polymer is obtained by a gel synthesis process. 11. The process according to claim 1 , wherein the composition additionally comprises water and/or ethanol. 12. The process according to claim 1 , wherein the polymer is obtained from at least 50 mol % of at least one non-ionic monomer selected from the group consisting of N-substituted acrylamides, N-substituted methacrylamides, N,N-substituted acrylamides, and N,N-substituted methacrylamides. 13. The process according to claim 1 , wherein the ethanol is bioethanol. 14. The process according to claim 2 , wherein the at least one monomer has a substituted chain containing at least 30 carbon atoms. 15. The process according to claim 2 , wherein the N-substituted acrylamide monomers, N-substituted methacrylamide monomers, N,N-substituted acrylamide monomers and N,N-substituted methacrylamide monomers are selected from the group consisting of N-ethylacrylamide, N-isopropylacrylamide, N-tert-Butylacrylamide, Diacetoneacrylamide, N-hydroxyethylacrylamide, N-hydroxymethylacrylamide, N-alkyl acrylamide, N-[Tris(hydroxymethyl)methyl]acrylamide, N-acryloylmorpholine, N,N-Dimethylacrylamide, N,N-diethylacrylamide and N,N-dialkylacrylamide; alkyl representing an alkyl group comprising 3 to 22 carbon atoms. 16. The process according to claim 2 , wherein the substituted acrylate monomers and substituted methacrylate monomers are selected from the group consisting of methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, methyl methacrylate, ethyl methacrylate, propyl methacrylate, butyl methacrylate, other alkyl acrylate, alkyl methacrylate, isobornyl acrylate, isobornyl methacrylate, 2-ethylhexyl acrylate, 2-ethylhexyl methacrylate, Hydroxyethyl acrylate, Hydroxyethyl methacrylate, hydroxypropyl acrylate, hydroxypropyl methacrylate, furfuryl acrylate, furfuryl methacrylate, tetrahydrofurfuryl acrylate, tetrahydrofurfuryl methacrylate, glyceryl acrylate, glyceryl methacrylate, glycidyl acrylate, and glycidyle methacrylate; alkyl representing an alkyl group comprising 5 to 22 carbon atoms. 17. The process according to claim 2 , wherein the polymer additionally includes at least 40 mol % of at least one ionic monomer. 18. The process according to claim 17 , wherein the ionic monomer is an anionic monomer selected from the group consisting of acrylic acid, methacrylic acid, itaconic acid, maleic acid, and 2-Acrylamido-2-methylpropane sulfonic acid (ATBS), the said anionic monomer being in its acid form, salified either partially or completely. 19. The process according to claim 18 , wherein the polymer includes at least 80 mol % of the at least one monomer selected from the group consisting of N-substituted acrylamides, N-substituted methacrylamides, N,N-substituted acrylamides, N,N-substituted methacrylamides, substituted acrylates and substituted methacrylates. 20. The process according to claim 19 , wherein the polymer is a polymer selected from the group consisting of N,N-dimethylacrylamide homopolymer, N,N-diethylacrylamide homopolymer, N,N-dimethylacrylamide copolymer and acrylic acid copolymer, N,N-diethylacrylamide copolymer and acrylic acid copolymer, N,N-dimethylacrylamide copolymer and 2-Acrylamido-2-methylpropane sulfonic acid copolymer and N,N-diethylacrylamide copolymer and 2-Acrylamido-2-methylpropane sulfonic acid copolymer.

Assignees

Inventors

Classifications

  • mono-carboxylic · CPC title

  • homo- or copolymers derived from unsaturated compounds containing amide and/or imide groups (C10L1/221 takes precedence) · CPC title

  • for improving storage or transport of the fuel · CPC title

  • C10M151/02Primary

    Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds · CPC title

  • Additive or component is a polymer · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US9822325B2 cover?
This invention involves a process for reducing friction in ethanol during its transport through pipelines. This process involves combining ethanol with a polymer-based composition, characterized in that the polymer is obtained from at least 50 mol % of at least one monomer selected from the group comprising N-substituted acrylamides, N-substituted methacrylamides, N,N-substituted acrylamides, N…
Who is the assignee on this patent?
Spcm Sa
What technology area does this patent fall under?
Primary CPC classification C10M151/02. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Nov 21 2017 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 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).