Sectional isobaric ammonia synthesis process
A technology of ammonia synthesis and ammonia synthesis tower, which is applied in the field of ammonia synthesis, can solve the problems of low utilization rate of nitrogen and hydrogen, low net value of exported ammonia, etc., and achieve the effects of reducing energy consumption, improving activity of ammonia synthesis, and improving stability
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Embodiment 1
[0053] The present embodiment provides a segmented isobaric ammonia synthesis process, comprising the following steps:
[0054] 1) The raw material gas for ammonia synthesis is obtained after desulfurization, shift, desulfurization, decarburization and refining of shift gas, wherein S2 <10ppm, the molar ratio of hydrogen to nitrogen is 1.7:1;
[0055] 2) the above-mentioned synthetic ammonia raw material gas is 5000h with space velocity -1 The primary ammonia synthesis is carried out in the first ammonia synthesis tower filled with iron-based catalyst, the synthesis pressure of the primary ammonia synthesis is 6MPa, and the synthesis temperature is 450°C;
[0056] Wherein, the iron-based catalyst is Fe with a mass ratio of 2:2:1 3 o 4 , FeO and K 2 O is the active ingredient, with rare earth element oxides CeO and MgAl 2 o 4 As an auxiliary agent, the content of the active ingredient in the iron-based catalyst is 4wt%, the rare earth element oxide content is 0.1wt%, MgAl ...
Embodiment 2
[0065] The present embodiment provides a segmented isobaric ammonia synthesis process, comprising the following steps:
[0066] 1) The raw material gas for ammonia synthesis is obtained after desulfurization, shift, desulfurization, decarburization and refining of shift gas, wherein S2 <10ppm, the molar ratio of hydrogen to nitrogen is 1.5:1;
[0067] 2) The above-mentioned synthetic ammonia raw material gas is 6000h with space velocity -1 The primary ammonia synthesis is carried out in the first ammonia synthesis tower filled with iron-based catalyst, the synthesis pressure of the primary ammonia synthesis is 5MPa, and the synthesis temperature is 500°C;
[0068] Wherein, the iron-based catalyst is Fe with a mass ratio of 3:1:1 3 o 4 , FeO and K 2 O is the active ingredient, with rare earth element oxides CeO and MgAl 2 o 4 As an auxiliary agent, the content of the active ingredient in the iron-based catalyst is 2wt%, the rare earth element oxide content is 0.2wt%, MgAl ...
Embodiment 3
[0077] The present embodiment provides a segmented isobaric ammonia synthesis process, comprising the following steps:
[0078] 1) The raw material gas for ammonia synthesis is obtained after desulfurization, shift, desulfurization, decarburization and refining of shift gas, wherein S2 <10ppm, the molar ratio of hydrogen to nitrogen is 2.5:1;
[0079] 2) The above-mentioned synthetic ammonia raw material gas is 4000h with space velocity -1 The primary ammonia synthesis is carried out in the first ammonia synthesis tower filled with iron-based catalyst, the synthesis pressure of the primary ammonia synthesis is 7MPa, and the synthesis temperature is 430°C;
[0080] Wherein, the iron-based catalyst is Fe with a mass ratio of 2.5:1.5:1 3 o 4 , FeO and K 2 O is the active component, with rare earth element oxides CeO and MgAl 2 o 4 As an auxiliary agent, the content of the active ingredient in the iron-based catalyst is 3wt%, the rare earth element oxide content is 0.15wt%, M...
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