Method for synthesizing low pressure ammonia
A low-pressure technology for ammonia synthesis, applied in the field of ammonia synthesis, can solve the problems of high energy consumption and high investment, and achieve the effects of reducing power consumption, simplifying equipment, and reducing hydrogen content
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Embodiment 1
[0030] see figure 1 , the raw material gas obtained from coal gasification, or the tail gas produced by alcohol and ether, or the tail gas of coke oven, or the tail gas of steelmaking and the reformed natural gas with an operating pressure of 0.7-4.0MPa, is boosted by "compression 1" Finally, carry out desulfurization, conversion, decarburization, and then "compression 2" to raise the pressure to 10MPa and then enter the gas preheater, and exchange heat with the hot synthesis gas from the bottom of the synthesis tower before entering the synthesis tower. 10.0MPa, air speed 9000h -1 , the temperature is 300-400°C, and the hydrogen-nitrogen ratio of the feed gas is 0.55. The composition of gas entering and exiting the tower in the ammonia synthesis process is shown in Table 1.
[0031] Table 1
[0032] Composition / %
Embodiment 2
[0034] Repeat the process of Example 1, the feed gas hydrogen-nitrogen ratio is 1.11, space velocity 10000h -1 , temperature 300 ~ 400 ℃. The composition of gas entering and exiting the tower in the ammonia synthesis process is shown in Table 2.
[0035] Table 2
[0036] Composition / %
Embodiment 3
[0038] Repeat the process of Example 1, the feed gas hydrogen-nitrogen ratio is 1.46, space velocity 10000h -1 , temperature 300 ~ 400 ℃. The composition of gas entering and exiting the tower in the ammonia synthesis process is shown in Table 3.
[0039] table 3
[0040] Composition / %
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