Process for the selective hydrogenation and hydrodesulferization of a pyrolysis gasoline feedstock
US-9260670-B2 · Feb 16, 2016 · US
US9533924B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9533924-B2 |
| Application number | US-201214008464-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 30, 2012 |
| Priority date | Mar 31, 2011 |
| Publication date | Jan 3, 2017 |
| Grant date | Jan 3, 2017 |
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A method for producing a hydrocarbon material from a C 5 raffinate which is obtained as an extracted residual oil after separating at least part of the isoprene by extraction distillation from a C 5 fraction which is produced as a byproduct when thermally cracking naphtha to produce ethylene and has C 5 organic compounds as main ingredients comprising, a gas-phase thermal cracking step of gasifying the C 5 raffinate to thermally crack at least part of the C 10 diolefins which are contained in the gasified C 5 raffinate, a desulfurization step, after the gas-phase thermal cracking step, of removing at least part of the sulfur-containing ingredients which are contained in the gasified C 5 raffinate after the gas-phase thermal cracking step in the gas-phase state, and a hydrogen addition step, after the desulfurization step, of hydrogenating at least part of the carbon-carbon double bonds of at least one selected from diolefins and olefins which are contained in the gasified C 5 raffinate after the desulfurization step in the gas-phase state, so as to obtain a hydrocarbon material with a total concentration of diolefins and olefins of 0.5 wt % or less is provided.
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The invention claimed is: 1. A method for producing a hydrocarbon material from a C 5 raffinate which is obtained as an extracted residual oil after separating at least part of isoprene by extraction distillation from a C 5 fraction which is produced as a byproduct when thermally cracking naphtha to produce ethylene and has C 5 organic compounds as main ingredients comprising, a gas-phase thermal cracking step of gasifying said C 5 raffinate which contains dicyclopentadiene in 10 wt % or more to thermally crack at least part of C 10 diolefins which are contained in the gasified C 5 raffinate, a desulfurization step, after said gas-phase thermal cracking step, of removing at least part of the sulfur-containing ingredients which are contained in the gasified C 5 raffinate after said gas-phase thermal cracking step in the gas-phase state, and a hydrogen addition step, after said desulfurization step, of hydrogenating at least part of the carbon-carbon double bonds of at least one selected from diolefins and olefins which are contained in the gasified C 5 raffinate after said desulfurization step in the gas-phase state, so as to obtain a hydrocarbon material with a total concentration of diolefins and olefins of 0.5 wt % or less, wherein said desulfurization step is performed in a reducing atmosphere under conditions of a pressure of 0.3 MPa or less and a temperature of 180 to 400° C. 2. The method for producing a hydrocarbon material as set forth in claim 1 wherein said desulfurization step is performed using a catalyst having a supported nickel as a main ingredient. 3. The method for producing a hydrocarbon material as set forth in claim 1 wherein said hydrogen addition step is performed in a reducing atmosphere under conditions of a pressure of 0.3 MPa or less and a temperature of 140 to 400° C. 4. The method for producing a hydrocarbon material as set forth in claim 1 wherein said hydrogen addition step is performed using a catalyst having a supported nickel as a main ingredient. 5. A hydrocarbon material which is obtained by the method as set forth in claim 1 . 6. The hydrocarbon material as set forth in claim 5 which is a raw material for an ethylene cracker. 7. The hydrocarbon material as set forth in claim 5 which is used as a gasoline base material.
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