Bio-assisted process for conversion of mixed volatile fatty acids to selective drop-in fuels

Patent metadata

Field	Value
Publication number	US-2019284584-A1
Application number	US-201916353666-A
Country	US
Kind code	A1
Filing date	Mar 14, 2019
Priority date	Mar 15, 2018
Publication date	Sep 19, 2019
Grant date	—

Abstract

The present invention relates to a two-stage process for production of drop-in fuels/alcohols (methanol, ethanol or butanol) from volatile fatty acids produced either synthetically from fossil resources or as metabolic intermediates in acidification step of anaerobic digestion process from waste biomass and organic materials.

First claim

1 . A bio-assisted process for production of drop-in fuels from CO 2 and volatile fatty acid rich source, said process comprising:
(a) providing, a first electrochemical system comprising at least one working electrode, at least one counter electrode, and a medium inoculated with selectively enriched electro-active bacteria selected from the group consisting of Geobacter anodireducens, Clostridium ljungdahlii, Acetobacterium woodii, Sporomusa acidovorans, Propionibacterium acidifaciens, Acetobacterium carbinolicum, Pseudomonas stutzeri (MTCC 25027), Pseudomonas fragi (MTCC 25025), Pseudomonas aeruginosa (MTCC, 5389), Psuedomonas alcaligenes, Schewanella putrefaciens, Clostridium aciditolerans, Enterobacter aerogenes (MTCC 25016) Shewanella sp. (MTCC 25020), and combinations thereof; (b) providing, feedstock to the first electrochemical system of step (a), wherein the feedstock comprises CO 2 with or without the volatile fatty acid rich source; (c) intensifying carboxylic acids in the feedstock of step (b) to obtain an effluent comprising intensified carboxylic acids; (d) providing a second electrochemical system comprising at least one working electrode, at least one counter electrode, and a medium inoculated with selectively enriched electro-active bacteria selected from the group consisting of Sporomusa ovate, Clostridium acetobutylicum, Clostridium butyricum, Clostridium acidurici, Pseudomonas aeruginosa (MTCC 5388), Pseudomonas putida (MTCC 5387), Clostridium carboxidivorans, Clostridium beijerinckii, Schewanella oneidensis, Geobacter sulfurreducens, Clostridium cellutolyticum, Clostridium cellulosi, Clostridium cellulovorans, Alicaligens sp. (MTCC 25022), Serratia sp. (MTCC 25017), Lysinibacillus sp. (MTCC 5666), and combinations thereof; and (e) reducing the intensified carboxylic acids of step (c) in the second electrochemical system to obtain the drop-in fuels;
wherein the working electrode of the first electrochemical system is composed of a material selected from the group consisting of graphite plate, carbon brush, carbon paper, graphite felt, activated carbon cloth, and combinations thereof;
wherein the counter electrode of the first electrochemical system is modified with a material selected from the group consisting of CNT, graphene, charcoal, activated carbon, SS mesh, nickel oxide, zinc oxide, and iron oxide;
wherein the volatile fatty acid rich source comprises at least 0.5% formic acid, provided that if the formic acid is not already present in the feedstock the feedstock is supplemented with at least 0.5% formic acid;
wherein the working electrode of the second electrochemical system is composed of a material selected from the group consisting of graphite plate, graphite rod, carbon brush, carbon paper, carbon plate, graphite felt, activated carbon cloth, and combinations thereof; and
wherein the counter electrode of the second electrochemical system is modified with a material selected from the group consisting of CNT, Co 9 S 8 , graphene, FTO/NiO, Ni/Fe layered double hydroxide, Si/TiO 2 nanowires, charcoal, activated carbon, nickel oxide, zinc oxide, and iron oxide.

2 . The bio-assisted process as claimed in claim 1 , wherein the first electrochemical system is operated at a temperature ranging from 20° C. to 50° C.

3 . The bio-assisted process as claimed in claim 1 , wherein the first electrochemical system is operated at a pH ranging from 6.5 to 9.0.

4 . The bio-assisted process as claimed in claim 1 , wherein the first electrochemical system is operated at an applied potential ranging from 1 V to 4 V.

5 . The bio-assisted process as claimed in claim 1 , wherein the working electrode of the second electrochemical system is modified with a material selected from the group consisting of CNT, graphene, activated charcoal, noble metal, composite of Zr or Ti or Cd or Fe, metal-free alloy, metal carbide, phosphide, and nickel oxide, zinc oxide, iron oxide, metal-phosphorous alloy, metal-sulfur alloy, metal organic framework, and combinations thereof.

6 . The bio-assisted process as claimed in claim 1 , wherein the carboxylic acid in step has a length ranging from C2 to C6.

7 . The bio-assisted process as claimed in claim 1 , wherein the second electrochemical system is operated at a temperature ranging from 20° C. to 50° C.

8 . The bio-assisted process as claimed in claim 1 , wherein the second electrochemical system is operated at a pH ranging from 4.0 to 6.0.

9 . The bio-assisted process as claimed in claim 1 , wherein the second electrochemical system is operated at an applied potential ranging from 2 V to 6 V.

10 . The bio-assisted process as claimed in claim 1 , wherein the volatile fatty acid rich source is selected from the group consisting of kitchen waste, biomass waste, agricultural waste, biodegradable municipal waste, lignocellulosic waste, and de-oiled algal cake.

11 . The bio-assisted process as claimed in claim 1 , wherein the reduction of carboxylic acids in step (e) is carried out in presence of a redox shuttler selected from the group consisting of neutral red, methylene blue, phenazine derivative, iron based metal complex, nickel based metal complex, zinc based metal complex, AQDS, and combinations thereof.

12 . The bio-assisted process as claimed in claim 1 , wherein the drop-in fuels are selected from the group consisting of methanol, ethanol, butanol, formic acid, acetic acid, propanoic acid, butanoic acid, valeric acid, and caproic acid.

Assignees

• Indian Oil Corp Ltd

Inventors

• Kumar Manoj
• Srikanth Sandipam
• Singh Dheer
• Puri Suresh Kumar
• RAMAKUMAR Sankara Sri Venkata

Classifications

• C10L2290/38

  Applying an electric field or inclusion of electrodes in the apparatus · CPC title

• C10L1/02

  essentially based on components consisting of carbon, hydrogen, and oxygen only · CPC title

• C12P7/14 Primary

  Multiple stages of fermentation; Multiple types of microorganisms or re-use of microorganisms · CPC title

• C10L2290/26

  Composting, fermenting or anaerobic digestion fuel components or materials from which fuels are prepared · CPC title

• C10L2200/0484

  Vegetable or animal oils · CPC title