Catalyst for coproduction of synthesis gas prepared gasoline and low carbon olefin and preparation method of catalyst
The invention discloses a catalyst for coproduction of synthesis gas prepared gasoline and low carbon olefin and a preparation method of the catalyst. The preparation method of the catalyst comprisesthe following steps that (1) EDTA, EDTA2Na and Fe(NO3)3.9H2O are added into water, a uniform Fe-EDTA-...
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| creator | DAI TIANFU MA XIAOXUN BI WENFEI HU BAIRUI DAI CHENGYI DU KANG ZHAO XIAO |
| description | The invention discloses a catalyst for coproduction of synthesis gas prepared gasoline and low carbon olefin and a preparation method of the catalyst. The preparation method of the catalyst comprisesthe following steps that (1) EDTA, EDTA2Na and Fe(NO3)3.9H2O are added into water, a uniform Fe-EDTA-EDTA2Na complexing solution without precipitates is prepared, in the complexing solution, the content of Fe is 10wt% of the weight of a gamma-Al2O3 carrier, and the molar ratio of Fe to the EDTA to the EDTA2Na is 2:1:1; (2) the gamma-Al2O3 carrier is added into the Fe-EDTA-EDTA2Na complexing solution, after uniform mixing, drying is conducted for staying overnight, and thus a solid is obtained; (3) the solid is ground into powder; and (4) the powder is roasted for 4-6 h at the temperature of 500-600 DEG C, and thus Fe-Na/gamma-Al2O3 powder is obtained. The catalyst for coproduction of the synthesis gas prepared gasoline and the low carbon olefin and the preparation method of the catalyst have the beneficial effects |
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The preparation method of the catalyst comprisesthe following steps that (1) EDTA, EDTA2Na and Fe(NO3)3.9H2O are added into water, a uniform Fe-EDTA-EDTA2Na complexing solution without precipitates is prepared, in the complexing solution, the content of Fe is 10wt% of the weight of a gamma-Al2O3 carrier, and the molar ratio of Fe to the EDTA to the EDTA2Na is 2:1:1; (2) the gamma-Al2O3 carrier is added into the Fe-EDTA-EDTA2Na complexing solution, after uniform mixing, drying is conducted for staying overnight, and thus a solid is obtained; (3) the solid is ground into powder; and (4) the powder is roasted for 4-6 h at the temperature of 500-600 DEG C, and thus Fe-Na/gamma-Al2O3 powder is obtained. 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The preparation method of the catalyst comprisesthe following steps that (1) EDTA, EDTA2Na and Fe(NO3)3.9H2O are added into water, a uniform Fe-EDTA-EDTA2Na complexing solution without precipitates is prepared, in the complexing solution, the content of Fe is 10wt% of the weight of a gamma-Al2O3 carrier, and the molar ratio of Fe to the EDTA to the EDTA2Na is 2:1:1; (2) the gamma-Al2O3 carrier is added into the Fe-EDTA-EDTA2Na complexing solution, after uniform mixing, drying is conducted for staying overnight, and thus a solid is obtained; (3) the solid is ground into powder; and (4) the powder is roasted for 4-6 h at the temperature of 500-600 DEG C, and thus Fe-Na/gamma-Al2O3 powder is obtained. 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The preparation method of the catalyst comprisesthe following steps that (1) EDTA, EDTA2Na and Fe(NO3)3.9H2O are added into water, a uniform Fe-EDTA-EDTA2Na complexing solution without precipitates is prepared, in the complexing solution, the content of Fe is 10wt% of the weight of a gamma-Al2O3 carrier, and the molar ratio of Fe to the EDTA to the EDTA2Na is 2:1:1; (2) the gamma-Al2O3 carrier is added into the Fe-EDTA-EDTA2Na complexing solution, after uniform mixing, drying is conducted for staying overnight, and thus a solid is obtained; (3) the solid is ground into powder; and (4) the powder is roasted for 4-6 h at the temperature of 500-600 DEG C, and thus Fe-Na/gamma-Al2O3 powder is obtained. The catalyst for coproduction of the synthesis gas prepared gasoline and the low carbon olefin and the preparation method of the catalyst have the beneficial effects</abstract><oa>free_for_read</oa></addata></record> |
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| subjects | CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY CHEMISTRY CRACKING HYDROCARBON OILS FUELS LUBRICANTS METALLURGY MINERAL WAXES PEAT PERFORMING OPERATIONS PETROLEUM, GAS OR COKE INDUSTRIES PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS REFORMING OF NAPHTHA TECHNICAL GASES CONTAINING CARBON MONOXIDE THEIR RELEVANT APPARATUS TRANSPORTING |
| title | Catalyst for coproduction of synthesis gas prepared gasoline and low carbon olefin and preparation method of catalyst |
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