Method for creating high carbon content products from biomass oil
In a method for producing high carbon content products from biomass, a biomass oil is added to a cracking reactor vessel. The biomass oil is heated to a temperature ranging from about 100° C. to about 800° C. at a pressure ranging from about vacuum conditions to about 20,700 kPa for a time sufficient to crack the biomass oil. Tar is separated from the cracked biomass oil. The tar is heated to a temperature ranging from about 200° C. to about 1500° C. at a pressure ranging from about vacuum conditions to about 20,700 kPa for a time sufficient to reduce the tar to a high carbon content product containing at least about 50% carbon by weight.
1. A method for producing high carbon content products from biomass, the method comprising:
adding a biomass oil to a cracking reactor vessel;
cracking the biomass oil in the cracking reactor vessel at a temperature ranging from 100° C. to 800° C. at a pressure ranging from vacuum conditions to 20,700 kPa (3000 psia) for a time sufficient to crack the biomass oil;
separating tar from cracked biomass oil; and
heating the tar to a temperature ranging from 200° C. to 1500° C. at a pressure ranging from vacuum conditions to 20,700 kPa (3000 psia) for a time sufficient to reduce the tar to a high carbon content product containing at least 50% carbon by weight.
2. The method of claim 1 , wherein the high carbon content product contains at least 70% carbon by weight.
3. The method of claim 1 , wherein the high carbon content product contains at least 90% carbon by weight.
4. The method of claim 1 , wherein the step of separating tar from cracked biomass oil is selected from the group consisting of solvent extraction, distillation, reactive distillation, evaporation, membrane separation, chemical reaction and combinations thereof.
5. The method of claim 1 , wherein the biomass oil is selected from the group consisting of plant oil, microbial lipid, animal fat, triacylglycerides, long chain fatty acids, long chain lipids and combinations thereof.
6. The method of claim 5 , wherein the biomass oil is a plant oil selected from the group consisting of soybean oil, canola oil, palm oil, sunflower oil, corn oil, flaxseed oil, jatropha oil, cottonseed oil, safflower oil, crambe oil, evening primrose oil, sesame oil, rapeseed oil, olive oil, coconut oil, camelina oil, jojoba oil, and combinations thereof.
7. The method of claim 1 , wherein the biomass oil is heated in the cracking reactor vessel to a temperature ranging from 300° C. to 700° C.
8. The method of claim 1 , wherein the biomass oil is heated in the cracking reactor vessel for up to 500 minutes.
9. The method of claim 1 , wherein the biomass oil is heated in the cracking reactor vessel with a gas selected from the group consisting of an inert gas, nitrogen, water vapor, hydrogen, a mixture of vapor-phase organic chemicals and combinations thereof.
10. The method of claim 1 , wherein a catalyst selected from the group consisting of alumina, silica-alumina, sulfated metal oxides, zeolites, palladium, niobium, molybdenum, platinum, titanium, aluminum, cobalt, gold and combinations thereof is added to the cracking reactor vessel.
11. The method of claim 1 , wherein the tar is heated to a temperature ranging from 400° C. to 800° C.
12. The method of claim 1 , wherein the tar is heated for up to 500 minutes.
13. The method of claim 1 , wherein the tar is heated with a gas selected from the group consisting of an inert gas, nitrogen, water vapor, hydrogen, a mixture of vapor-phase organic chemicals and combinations thereof.
14. The method of claim 1 , further comprising:
processing the high carbon content product into activated carbon or carbon black.
15. A method for producing a high carbon content product, short chain carboxylic acids and a fuel composition having a low cloud point from biomass, the method comprising:
cracking a biomass oil in a reactor vessel at a temperature ranging from 100° C. to 800° C. and a pressure ranging from vacuum conditions to 20,700 kPa (3000 psia) for a time sufficient to crack the biomass oil;
collecting fractions of cracked biomass oil including at least one of C4 to C16 alkanes, alkenes, aromatics, cycloparaffins, or alcohols; C2 to C16 fatty acids; or C2 to C16 fatty acid methyl esters and combining collected fractions of cracked biomass oil to produce a fuel composition having a cloud point less than −10° C.;
collecting a mixture from the cracked biomass oil containing C2 to C16 carboxylic acids; and
separating tar from the cracked biomass oil and heating the tar to a temperature ranging from 200° C. to 1500° C. at a pressure ranging from vacuum conditions to 20,700 kPa (3000 psia) for a time sufficient to reduce the tar to a high carbon content product containing at least 50% carbon by weight.
16. The method of claim 15 , wherein the biomass oil is selected from the group consisting of plant oil, microbial lipid, animal fat, triacylglycerides, long chain fatty acids, long chain lipids and combinations thereof.
17. The method of claim 15 , wherein the high carbon content product contains at least 70% carbon by weight.
18. The method of claim 1 , wherein the biomass oil is heated in the cracking reactor vessel in the absence of a catalyst.
19. The method of claim 15 , wherein the biomass oil is heated in the reactor vessel in the absence of a catalyst.
20. The method of claim 1 , wherein the high carbon content product containing at least 50% carbon by weight is free of catalysts.