Production of Xylenes From Syngas
US-2016024393-A1 · Jan 28, 2016 · US
US10442998B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10442998-B2 |
| Application number | US-201615735059-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 9, 2016 |
| Priority date | Jun 12, 2015 |
| Publication date | Oct 15, 2019 |
| Grant date | Oct 15, 2019 |
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A method and an apparatus for producing a chemical compound from biomass based raw material. The bio-mass based raw material is gasified in a gasification device for forming a gasification gas, the gasification gas is treated in the reactor which includes at least one catalyst layer including Fe-based catalyst for forming a hydrocarbon composition, at least one hydrocarbon fraction including olefins is recovered from the hydrocarbon composition, and a chemical compound is formed from the hydrocarbon fraction. Further, the invention relates to the produced chemical compound.
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The invention claimed is: 1. A method for producing a chemical compound from biomass based raw material, the method comprising: gasifying the biomass based raw material in a gasification device forming a gasification gas, treating the gasification gas in a reactor which has a catalyst layer consisting essentially of a Fe-based catalyst for forming a hydrocarbon composition, recovering at least one hydrocarbon fraction comprising olefins from the hydrocarbon composition so that the hydrocarbon fraction comprising: C3 and C4+ olefins and paraffines, C4 olefins and paraffines, and/or C6-C18 α-olefins, are separated from the hydrocarbon composition, and treating the separated hydrocarbon fraction forming a chemical compound, with a material selected from the group consisting of: aromatics, maleic anhydride and/or alkenyl succinic anhydride, and the treatment is carried out such that the hydrocarbon composition or the hydrocarbon fraction comprising C3 and C4+ olefins and paraffines is treated by an aromatization which is performed at normal pressure and in the presence of a zeolite catalyst for forming aromatics, and/or the hydrocarbon fraction comprising C4 olefins and paraffines is partially oxidized forming maleic anhydride. 2. The method according to claim 1 , wherein the reaction pressure in the gasification device is between 1-10 bar. 3. The method according to claim 1 , wherein the temperature of the catalyst layer is between 200-350° C. in the reactor. 4. The method according to claim 1 , wherein the hydrocarbon composition is condensated by water. 5. The method according to claim 1 , wherein the hydrocarbon composition is fractionated for recovering at least one hydrocarbon fraction comprising olefins. 6. The method according to claim 5 , wherein the fractionating of the hydrocarbon composition is performed by using distillation. 7. The method according to claim 1 , further comprising: treating the C3 and C4+ olefins and paraffines by an aromatization performed at normal pressure and in the presence of a zeolite catalyst for forming aromatics, separating a benzene fraction from the aromatics, and partially oxidizing the benzene fraction forming maleic anhydride. 8. The method according to claim 1 , wherein the hydrocarbon fraction comprising C6-C18 α-olefins is treated by a reaction with maleic anhydride so that olefins react with maleic anhydride for forming alkenyl succinic anhydride. 9. The method according to claim 1 , further comprising removing sulphur from the at least one hydrocarbon fraction in a sulphur removing bed using a second Fe-based catalyst or a modified Fe-based catalyst.
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