White alkanes created from non-petroleum, renewable sources
The present invention describes a method to produce high purity hydrocarbon materials and the high purity hydrocarbon materials produced from renewable sources. The produced materials are chemically similar and of equal or higher purity to from highly refined mineral oils and/or synthetic hydrocarbons. These renewable hydrocarbon materials can be used as a replacement for mineral and synthetic hydrocarbon base oils, process fluids, white oils in products such as lubricants, rubber, personal care, pharma.
1. A method of producing hydrocarbon material called a White Alkane, wherein said White Alkane is a hydrocarbon material derived from renewable sources and meets all or some of the requirements for being a white mineral oil as set forth in at least one of the European Pharmacopoeia (Ph. Eur.), United States Pharmacopeia (USP), National Formulary (NF), Japanese Pharmacopoeia (JP), or former monographs of the British Pharmacopoeia (BP), German Pharmacopoeia (also known as the Deutsches Arzneibuch) (DAB), or French Codex (also known as the Pharmacopée Française), comprising:
selecting a feed material, wherein said feed material contains renewable carbon, wherein said renewable carbon is not sourced from petroleum or crude oil, wherein said feed material renewable carbon is chosen from the group comprising: renewable diesel, biodiesel, vegetable oils, polymerized vegetable oils, polymerized fatty acids, polymerized fatty acid esters, triglycerides, diglycerides, monoglycerides, organic esters, naturally occurring oil or material containing 50 % or more of unsaturated fatty acid components including mono-, di-, and tri-unsaturated hydrocarbon chains, soy, canola, castor, corn, cottonseed, crambe, linseed, olive, peanut, rapeseed, safflower, sunflower, tall oil fatty acid, coconut, palm; oils derived from seeds, pulp, beans, legumes, rinds, pits or any part of an oil bearing fraction of the intended plant; animal fats or fish oils, or a mixture thereof;
hydro-decarboxylating said feed material;
hydro-deoxygenating said feed material; and
wherein either said white alkane or a first intermediate is produced.
2. The method of claim 1 , further comprising:
separating said first intermediate into different components, and removing wax, linear alkanes, or light boiling alkanes from said first intermediate, wherein said separating step is accomplished by at least one of: solvent dewaxing, urea dewaxing, distilling, fractionating, fractional crystallization, or light fraction stripping;
isomerizing said first intermediate;
purifying said first intermediate, wherein said purifying step is accomplished by at least one of: hydro-finishing, applying sulfur trioxide, applying oleum, sulfuric acid washing, bauxite filtration, clay-gel extraction, bentonite clay filtration, palygorskite mineral filtration, kaolin clay filtration, or activated carbon filtration; and
wherein said white alkane is produced.
3. The method of claim 1 , further comprising:
separating said first intermediate into different components, and removing wax, linear alkanes, or light boiling alkanes from said first intermediate, wherein said separating step is accomplished by at least one of: solvent dewaxing, urea dewaxing, distilling, fractionating, fractional crystallization, or light fraction stripping;
isomerizing said first intermediate; and
wherein either said white alkane or a second intermediate is produced.
4. The method of claim 3 , further comprising:
purifying said second intermediate, wherein said purifying step is accomplished by at least one of: hydro-finishing, applying sulfur trioxide, applying oleum, sulfuric acid washing, bauxite filtration, clay-gel extraction, bentonite clay filtration, palygorskite mineral filtration, kaolin clay filtration, or activated carbon filtration; and
wherein said White Alkane is produced.
5. The method of claim 1 , further comprising:
separating said first intermediate into different components, and removing wax, linear alkanes, or light boiling alkanes from said first intermediate, wherein said separating step is accomplished by at least one of: solvent dewaxing, urea dewaxing, distilling, fractionating, fractional crystallization, or light fraction stripping;
wherein either said white alkane or a second intermediate is produced.
6. The method of claim 5 , further comprising:
isomerizing said second intermediate; and
wherein either said white alkane or a third intermediate is produced.
7. The method of claim 6 , further comprising:
purifying said third intermediate, wherein said purifying step is accomplished by at least one of: hydro-finishing, applying sulfur trioxide, applying oleum, sulfuric acid washing, bauxite filtration, clay-gel extraction, bentonite clay filtration, palygorskite mineral filtration, kaolin clay filtration, or activated carbon filtration; and
wherein said White Alkane is produced.
8. The method of claim 1 , further comprising:
isomerizing said first intermediate; and
wherein either said white alkane or a second intermediate is produced.
9. The method of claim 8 , further comprising:
separating said second intermediate into different components, and removing wax, linear alkanes, or light boiling alkanes from said first intermediate, wherein said separating step is accomplished by at least one of: solvent dewaxing, urea dewaxing, distilling, fractionating, fractional crystallization, or light fraction stripping;
wherein either said white alkane or a third intermediate is produced.
10. The method of claim 9 , further comprising:
purifying said third intermediate, wherein said purifying step is accomplished by at least one of: hydro-finishing, applying sulfur trioxide, applying oleum, sulfuric acid washing, bauxite filtration, clay-gel extraction, bentonite clay filtration, palygorskite mineral filtration, kaolin clay filtration, or activated carbon filtration; and
wherein said White Alkane is produced.
11. The method of claim 3 , further comprising:
separating said second intermediate into different components, and removing wax, linear alkanes, or light boiling alkanes from said first intermediate, wherein said separating step is accomplished by at least one of: solvent dewaxing, urea dewaxing, distilling, fractionating, fractional crystallization, or light fraction stripping;
isomerizing said second intermediate; and
wherein either said white alkane or a third intermediate is produced.
12. The method of claim 11 , further comprising:
purifying said third intermediate, wherein said purifying step is accomplished by at least one of: hydro-finishing, applying sulfur trioxide, applying oleum, sulfuric acid washing, bauxite filtration, clay-gel extraction, bentonite clay filtration, palygorskite mineral filtration, kaolin clay filtration, or activated carbon filtration; and
wherein said white alkane is produced.
13. The method of claim 3 , further comprising:
separating said second intermediate into different components, and removing wax, linear alkanes, or light boiling alkanes from said first intermediate, wherein said separating step is accomplished by at least one of: solvent dewaxing, urea dewaxing, distilling, fractionating, fractional crystallization, or light fraction stripping; and
wherein either said white alkane or a third intermediate is produced.
14. The method of claim 13 , further comprising:
purifying said third intermediate, wherein said purifying step is accomplished by at least one of: hydro-finishing, applying sulfur trioxide, applying oleum, sulfuric acid washing, bauxite filtration, clay-gel extraction, bentonite clay filtration, palygorskite mineral filtration, kaolin clay filtration, or activated carbon filtration; and
wherein said white alkane is produced.
15. The method of claim 3 , further comprising:
isomerizing said second intermediate; and
wherein either said white alkane or a third intermediate is produced.
16. The method of claim 11 , further comprising:
purifying said third intermediate, wherein said purifying step is accomplished by at least one of: hydro-finishing, applying sulfur trioxide, applying oleum, sulfuric acid washing, bauxite filtration, clay-gel extraction, bentonite clay filtration, palygorskite mineral filtration, kaolin clay filtration, or activated carbon filtration; and
wherein said white alkane is produced.
17. A method of producing hydrocarbon material called a White Alkane, wherein said White Alkane is a hydrocarbon material derived from renewable sources and meets all or some of the requirements for being a white mineral oil as set forth in at least one of the European Pharmacopoeia (Ph. Eur.), United States Pharmacopeia (USP), National Formulary (NF), Japanese Pharmacopoeia (JP), or former monographs of the British Pharmacopoeia (BP), German Pharmacopoeia (also known as the Deutsches Arzneibuch) (DAB), or French Codex (also known as the Pharmacopée Française), comprising:
selecting a feed material, wherein said feed material contains renewable carbon, wherein said renewable carbon is not sourced from petroleum or crude oil, wherein said feed material renewable carbon is chosen from the group comprising: renewable diesel, biodiesel, vegetable oils, polymerized vegetable oils, polymerized fatty acids, polymerized fatty acid esters, triglycerides, diglycerides, monoglycerides, organic esters, naturally occurring oil or material containing 50% or more of unsaturated fatty acid components including mono-, di-, and tri-unsaturated hydrocarbon chains, soy, canola, castor, corn, cottonseed, crambe, linseed, olive, peanut, rapeseed, safflower, sunflower, tall oil fatty acid, coconut, palm; oils derived from seeds, pulp, beans, legumes, rinds, pits or any part of an oil bearing fraction of the intended plant; animal fats or fish oils, or a mixture thereof;
hydro-decarboxylating said feed material;
hydro-deoxygenating said feed material;
isomerizing said feed material;
separating said feed material into different components, and removing wax, linear alkanes, or light boiling alkanes from said first intermediate, wherein said separating step is accomplished by at least one of: solvent dewaxing, urea dewaxing, distilling, fractionating, fractional crystallization, or light fraction stripping;
purifying said feed material, wherein said purifying step is accomplished by at least one of: hydro-finishing, applying sulfur trioxide, applying oleum, sulfuric acid washing, bauxite filtration, clay-gel extraction, bentonite clay filtration, palygorskite mineral filtration, kaolin clay filtration, or activated carbon filtration; and
wherein said white alkane is produced.