Surface treated carbon catalysts produced from waste tires for fatty acids to biofuel conversion

Patent metadata

Field	Value
Publication number	US-2017342014-A1
Application number	US-201615163434-A
Country	US
Kind code	A1
Filing date	May 24, 2016
Priority date	May 24, 2016
Publication date	Nov 30, 2017
Grant date	—

Abstract

A method of making solid acid catalysts includes the step of sulfonating waste tire pieces in a first sulfonation step. The sulfonated waste tire pieces are pyrolyzed to produce carbon composite pieces having a pore size less than 10 nm. The carbon composite pieces are then ground to produce carbon composite powders having a size less than 50 μm. The carbon composite particles are sulfonated in a second sulfonation step to produce sulfonated solid acid catalysts. A method of making biofuels and solid acid catalysts are also disclosed.

First claim

1 . A method of making solid acid catalysts, comprising the steps of:
sulfonating the waste tire pieces in a first sulfonation step; pyrolyzing waste tire pieces to produce carbon composite pieces having a pore size less than 10 nm; grinding the carbon composite pieces to produce carbon composite particles having a particle size less than 50 μm; sulfonating the carbon composite particles in a second sulfonation step to produce sulfonated solid acid catalysts.

2 . The method of claim 1 , wherein at least one of the sulfonation steps is performed by soaking in a sulfuric acid bath.

3 . The method of claim 2 , wherein the sulfuric acid bath is at least 5 M.

4 . The method of claim 2 , wherein the sulfuric acid bath has a temperature of between −20° C. to 200° C.

5 . The method of claim 2 , wherein the soaking is for at least 10-20 minutes.

6 . The method of claim 1 , further comprising the step of washing the sulfonated waste tire pieces.

7 . The method of claim 6 , further comprising the step of pressing and heating the washed sulfonated waste tire pieces into a sheet prior to the pyrolyzing step.

8 . The method of claim 1 wherein the pyrolyzing step comprises heating the sulfonated waste tire pieces to from 900° C. to 1500° C.

9 . The method of claim 1 , wherein the second sulfonation step comprises contacting the carbon composite particles with L-cysteine with water and heat, followed by a reduction step and an oxidation step.

10 . The method of claim 1 , wherein the carbon composite particles have a size of from 2 μm to 20 μm.

11 . The method of claim 1 , wherein the carbon composite particles have a pore size of from 3 nm to 8 nm.

12 . A method of making biofuels, comprising the steps of:
preparing a solid acid catalyst, the solid acid catalyst being prepared by the steps of: a) sulfonating waste tire pieces in a first sulfonation step b) pyrolyzing the waste tire pieces to produce carbon composite pieces having a pore size less than 10 nm; c) grinding the carbon composite pieces to carbon composite particles having size less than 50 μm; and, d) sulfonating the carbon composite particles in a second sulfonation step to produce sulfonated solid acid catalysts; providing feedstock comprising free fatty acids; esterifying the free fatty acids in the presence of the sulfonated solid acid catalysts.

13 . The method of claim 12 , wherein the pyrolyzing step comprises heating the sulfonated waste tire pieces to from 900° C. to 1500° C.

14 . The method of claim 12 , wherein the esterification is performed in the presence of methanol.

15 . The method of claim 12 , wherein the free fatty acids comprise at least one selected from the group consisting of saturated and unsaturated free fatty acids.

16 . The method of claim 12 , wherein the free fatty acids comprise at least one selected from the group consisting of formic acid, acetic acid, oleic acid, linoleic acid, linolinic acid, palmitic acid, stearic acid, octadecadienoic acid, hexadecanoic acid, myristic acid, stearidonic acid, elaidic acid, gondoic acid, erucic acid, nervonic acid, mead acid, gadoleic acid, eicosenoic acid, erucic acid, pinolenic acid, stearidonic acid, arachidonic acid, eicosapentaenoic acid, and benzoic acid.

17 . The method of claim 12 , wherein the feedstock comprises at least one selected from the group consisting of animal fats, waste cooking oil, and vegetable oil.

18 . The method of claim 12 , wherein the second sulfonation step comprises contacting the carbon composite particles with L-cysteine using a hydrothermal method followed by a reduction step and an oxidation step to produce sulfonated solid acid catalysts.

19 . The method of claim 12 , wherein the carbon composite particles have a size of from 2 μm to 20 μm.

20 . The method of claim 12 , wherein the carbon composite particles have a pore size of from 3 nm to 8 nm.

21 . A solid acid catalyst, comprising:
an activated carbon particle of from 2 μm to 50 μm and having a plurality of pores having a pore size of from 1 nm to 10 nm; a plurality of sulfonic acid groups joined to all sides of the surface of the activated carbon particles.

22 . The solid acid catalyst of claim 21 , wherein the activated carbon particles have a size of from 2 μm to 20 μm.

Assignees

• Ut Battelle Llc

Inventors

• Hood Zachary D
• Adhikari Shiba P
• Wright Marcus W
• Lachgar Abdessadek
• Li Yunchao
• Naskar Amit K
• Paranthaman Mariappan Parans

Classifications

• B01J35/026

  Operations & Transport · mapped topic

• B01J2231/49

  Esterification or transesterification · CPC title

• B01J35/1057

  Operations & Transport · mapped topic

• B01J37/0072

  Preparation of particles, e.g. dispersion of droplets in an oil bath · CPC title

• B01J31/0225

  comprising sulfonic acid groups or the corresponding salts · CPC title