Process for converting a solid biomass material
US-9238779-B2 · Jan 19, 2016 · US
US10253268B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10253268-B2 |
| Application number | US-201414775949-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 14, 2014 |
| Priority date | Mar 15, 2013 |
| Publication date | Apr 9, 2019 |
| Grant date | Apr 9, 2019 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Described herein are methods for producing branched alkanes and branched alkenes from the pyrolysis of radical precursors.
Opening claim text (preview).
What is claimed: 1. A method for producing a fuel or solvent comprising a branched alkane, a branched alkene, or a combination thereof, comprising separately introducing (i) a fatty acid comprising a free fatty acid or a salt of a free fatty acid and (ii) one or more alkenes into a reactor and subsequently heating the fatty acid in the presence of the one or more alkenes at a temperature from 350° C. to 600° C. and a pressure from 130 to 2,000 psi in the reactor in the absence of any catalyst to produce the fuel or solvent. 2. A method for producing a fuel or solvent comprising a branched alkane, a branched alkene, or a combination thereof from a fatty acid comprising a free fatty acid or the salt of a free fatty acid, comprising separating the fatty acid from a fatty acid resource, introducing the fatty acid and one or more alkenes into a reactor, and subsequently heating the fatty acid in the presence of the one or more alkenes at a temperature from 350° C. to 600° C. and a pressure from 130 to 2,000 psi in the reactor in the absence of any catalyst to produce the fuel or solvent. 3. The method of claim 2 , wherein separating the fatty acid from the fatty acid resource comprises (a) separating one or more triglycerides from the fatty acid resource, (b) hydrolyzing the one or more triglycerides to produce the fatty acid, and (c) isolating the fatty acid. 4. The method of claim 2 , wherein the fatty acid resource comprises a monoglyceride, a diglyceride, a triglyceride, a lipid, a free fatty acid or salt thereof, or any combination thereof. 5. The method of claim 2 , wherein the fatty acid resource comprises vegetable oil, animal fats, spent cooking oil, lipids, phospholipids, triglycerides, or a bio-oil. 6. The method of claim 5 , wherein the fatty acid resource comprises vegetable oil, wherein the vegetable oil comprises corn oil, cottonseed oil, canola oil, rapeseed oil, olive oil, palm oil, peanut oil, ground nut oil, safflower oil, sesame oil, soybean oil, sunflower oil, algae oil, almond oil, apricot oil, argan oil, avocado oil, ben oil, cashew oil, castor oil, grape seed oil, hazelnut oil, hemp seed oil, linseed oil, mustard oil, neem oil, palm kernel oil, pumpkin seed oil, rice bran oil, walnut oil, tall oil, or a combination thereof. 7. The method of claim 5 , wherein the fatty acid resource comprises animal fats, wherein the animal fats comprise blubber, cod liver oil, ghee, lard, tallow, or a combination thereof. 8. The method of claim 1 or 2 , wherein the fatty acid comprises a saturated fatty acid, an unsaturated fatty acid, or a combination thereof. 9. The method of claim 1 or 2 , wherein the fatty acid comprises butyric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, alpha-linolenic acid, docosahexaenoic acid, eicosapentaenoic acid, linoleic acid, arachidonic acid, oleic acid, erucic acid, a naturally derived fatty acid from a plant or animal source, or a combination thereof. 10. The method of claim 1 or 2 , wherein the one or more alkenes is ethylene, propylene, butene or an isomer thereof, or any combination thereof. 11. The method of claim 1 or 2 , wherein the heating step is conducted at a temperature from 350° C. to 500° C. for two seconds up to 8 hours. 12. The method of claim 1 or 2 , wherein the heating step is conducted in the absence of supplemental hydrogen. 13. The method of claim 1 or 2 , wherein the fatty acid undergoes decarboxylation during said heating and wherein the rate of decarboxylation of the fatty acid is greater when heated in the presence of the one or more alkenes when compared to the same fatty acid that is heated under an inert atmosphere at the same reaction temperature and reaction time. 14. The method of claim 13 , wherein the inert atmosphere is nitrogen.
Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom (sulfonated fats or oils C07C309/62; factice C08H; drying oils C09F) · CPC title
of vegetal origin · CPC title
by distillation · CPC title
using bio-feedstock · CPC title
Thermal non-catalytic treatment · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.