Method of obtaining liquid biohydrocarbons from oils of natural origin
In the method of obtaining liquid biohydrocarbons from oils of natural origin, in the first step, the oil and/or waste oil is/are heated in the presence of a mixture of hydrogen and carbon monoxide in the presence of a catalyst in the form of a metal oxide selected from a group comprising CoO, NiO, MoO 3 , ZrO 2 , or a mixture of such metal oxides, on an oxide support selected from a group comprising SiO 2 , Al 2 O 3 , TiO 2 , whereupon the product of the first step is contacted with hydrogen gas or with a mixture of hydrogen and carbon monoxide in the presence of a metallic catalyst selected from a group comprising Pd, Pt, Co/Mo, Ni/Mo, Zr on an oxide support selected from a group comprising SiO 2 , Al 2 O 3 , TiO 2 , P 2 O 5 , ZrO 2 or on a mixture of such oxides.
1. A method of obtaining liquid biohydrocarbons from oils of natural origin, carried out in two steps in a coupled flow system in the presence of heterophase catalysts,
wherein in the first step,
the oils of natural origin are heated at a temperature in a range of 100-500° C.,
at a pressure in a range of 0.1-5 MPa in the presence of a mixture of hydrogen and carbon monoxide, and
in the presence of a catalyst in the form of a metal oxide selected from a group comprising CoO, NiO, MoO 3 , ZrO 2 , or a mixture of such metal oxides, on an oxide support selected from a group comprising SiO 2 , Al 2 O 3 , TiO 2 , thereby producing a product of the first step,
and wherein in the second step, the product of the first step is contacted with hydrogen gas or with a mixture of hydrogen and carbon monoxide
at a temperature in a range of 100-500° C.,
at a pressure in a range of 0.1-5 MPa, and
in the presence of a metallic catalyst selected from a group comprising Pd, Pt, Co/Mo, Ni/Mo, Zr on an oxide support selected from a group comprising SiO 2 , Al 2 O 3 , TiO 2 , P 2 O 5 , ZrO 2 or on a mixture of such oxides.
2. The method as claimed in claim 1 , wherein the catalyst used in the first step of the process is ZrO 2 or a mixture of ZrO 2 and one or more metal oxides selected from the group consisting of CoO, NiO, and MoO 3 .
3. The method as claimed in claim 1 , wherein the mixture of hydrogen and carbon monoxide used in the first and second steps of the process is a mixture obtained by a selective decomposition of methanol.
4. The method as claimed in claim 1 , wherein the first and/or second step of the process is/are carried out under atmospheric pressure.
5. The method of claim 1 , wherein the oils of natural origin are selected from the group consisting of vegetable oils, animal fats, algal oils and lipid fractions of ligno-cellulose waste.
6. The method of claim 1 , wherein the mixture of hydrogen and carbon monoxide is in a hydrogen to carbon monoxide molar ratio of 1 to 2.
7. The method of claim 1 , wherein the first step produces spatial isomers and/or hexamethylbenzene.
8. The method of claim 1 , wherein the first step produces 10-30% by weight of spatial isomers and/or 2-5% by weight of hexamethylbenzene in the product of the first step.
9. The method of claim 5 ,
wherein the mixture of hydrogen and carbon monoxide is in a hydrogen to carbon monoxide molar ratio of 1 to 2; and
wherein the first step produces 10-30% by weight of spatial isomers and/or 2-5% by weight of hexamethylbenzene in the product of the first step.
10. The method of claim 1 ,
wherein the first step consists essentially of:
heating oils of natural origin at a temperature in a range 100-500° C.,
at a pressure in a range 0.1-5 MPa in the presence of a mixture of hydrogen and carbon monoxide, and
in the presence of a catalyst in the form of a metal oxide selected from a group comprising CoO, NiO, MoO3, ZrO 2 , or a mixture of such metal oxides, on an oxide support selected from a group comprising SiO 2 , Al 2 O 3 , TiO 2 , thereby producing a product of the first step, and
wherein the second step consists essentially of:
the product of the first step is contacted with hydrogen gas or with a mixture of hydrogen and carbon monoxide,
at a temperature in a range of 100-500° C.,
at a pressure in a range of 0.1-5 MPa, and
in the presence of a metallic catalyst selected from a group comprising Pd, Pt, Co/Mo, Ni/Mo, Zr on an oxide support selected from a group comprising SiO 2 , Al 2 O 3 , TiO 2 , P 2 O 5 , ZrO 2 or on a mixture of such oxides.
11. The method of claim 10 , wherein the oils of natural origin are selected from the group consisting of vegetable oils, animal fats, algal oils and lipid fractions of ligno-cellulose waste.
12. The method of claim 10 ,
wherein the mixture of hydrogen and carbon monoxide is in a hydrogen to carbon monoxide molar ratio of 1 to 2; and
wherein the first step produces 10-30% by weight of spatial isomers and/or 2-5% by weight of hexamethylbenzene in the product of the first step.