Technique for synthesizing natural gas from coke oven gas by sulfur-resistant methanation
A technology resistant to sulfur methanation and coke oven gas, applied in the petroleum industry, gas fuel, fuel and other directions, can solve the problems of affecting the natural gas yield, waste of resources and environment, and large differences in composition, saving equipment investment and energy consumption , The effect of less equipment investment, reducing equipment investment and energy consumption
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Embodiment 1
[0032] In this embodiment, the catalyst used in the sulfur-tolerant methanation reactor I and the sulfur-tolerant methanation reactor II is the same, and its mass composition is MoO 3 13wt%-ZrO 2 14.5wt% / γ-Al 2 o 3 72.5 wt% catalyst, active component MoO 3 and additive ZrO 2 Loaded on γ-Al by co-precipitation 2 o 3 Above, see CN103480362A embodiment 7 for specific preparation method and technique; The mass composition of the nickel-based catalyst in the methanation reactor is NiO40wt%-La 2 o 3 7wt%-Al 2 o 3 43wt% - ZrO 2 7wt%, see CN102029162A Example 5 for the specific preparation method and steps. Adopt above-mentioned catalyzer, its concrete technological process and condition are as follows:
[0033] (1) After deoiling, deamination, debenzene and naphthalene removal, it is composed of H 2 50%, CO8%, CO 2 4%, CH 4 27%, N 2 7% and C 2-4 The coke oven gas with 4% hydrocarbons first passes through the inlet and outlet heat exchanger II to exchange heat with the...
Embodiment 2
[0038] In this embodiment, the catalyst used in the sulfur-tolerant methanation reactor I and the sulfur-tolerant methanation reactor II is the same, and its mass composition is MoO 3 35wt%-Co 2 o 3 +KO 2 2wt% / ZrO 2 63 wt% catalyst, active component MoO 3 and additive Co 2 o 3 +KO 2 Loaded on the carrier ZrO by impregnation 2 For the specific preparation method and process, see Example 14 of CN103495421A; the nickel-based catalyst in the methanation reactor adopts Davy's CEG-LH catalyst. Adopt above-mentioned catalyzer, its concrete technological process and condition are as follows:
[0039] (1) After deoiling, deamination, debenzene and naphthalene removal, it is composed of H 2 53.8%, CO7.3%, CO 2 3.7%, CH 4 25%, N 2 6.7% and C 2-4 The coke oven gas with 3.5% hydrocarbons first passes through the inlet and outlet heat exchanger II to exchange heat with the outlet gas of the sulfur-resistant methanation reactor II, and then through the inlet and outlet heat exch...
Embodiment 3
[0044] In this example, the catalysts used in sulfur-tolerant methanation reactor I and sulfur-tolerant methanation reactor II are the same, and the mass composition of the oxide is MoO 3 30wt%-Co 2 o 3 +Fe 2 o 3 +NiO20wt% / CeO 2 -Al 2 o 3 50 wt% catalyst, active component MoO 3 and additive Co 2 o 3 +Fe 2 o 3 +NiO is loaded on the carrier CeO by impregnation 2 -Al 2 o 3 Above, see CN102463118A embodiment 5 for specific preparation method and technique; The mass composition of the nickel-based catalyst in the methanation reactor is NiO75wt%-La 2 o 3 7wt%-Al 2 o 3 15wt% - ZrO 2 3wt%, see CN102029162A Example 4 for the specific preparation method and steps. Adopt above-mentioned catalyzer, its concrete technological process and condition are as follows:
[0045] (1) After deoiling, deamination, debenzene and naphthalene removal, it is composed of H 2 54.7%, CO6.9%, CO 2 3.5%, CH 4 25.6%, N 2 6.1% and C 2-4 The coke oven gas with 3.2% hydrocarbons first exc...
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