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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

Active Publication Date: 2017-09-26
BEIJING SJ ENVIRONMENTAL PROTECTION & NEW MATERIAL CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] Therefore, the technical problem to be solved by the present invention is to overcome the defects in the prior art that the outlet ammonia net value is not high and the utilization rate of nitrogen and hydrogen is low, and then provide a high outlet ammonia net value, high nitrogen and hydrogen utilization rate, low energy Low energy consumption and stable operation of staged isobaric ammonia synthesis process

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  • Sectional isobaric ammonia synthesis process
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  • Sectional isobaric ammonia synthesis process

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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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Abstract

The invention provides a sectional isobaric ammonia synthesis process. The sectional isobaric ammonia synthesis process comprises the following steps: (1) primary ammonia synthesis is performed on feed gases of synthetic ammonia in a first ammonia synthesis tower filled with an iron-based catalyst,wherein the synthetic pressure of the primary ammonia synthesis is 5-7 MPa, and the molar ratio of hydrogen to nitrogen in the feed gases of synthetic ammonia is (1.5-2.5):1; and (2) a mixed gas getting out of the first ammonia synthesis tower enters a second ammonia synthesis tower filled with a ruthenium-based catalyst to perform secondary ammonia synthesis, wherein the synthetic pressure of the secondary ammonia synthesis is 4-6 MPa. According to the sectional isobaric ammonia synthesis process, as the ammonia synthesis process is divided into two stages and performed under the specific pressures, specific catalysts and the specific hydrogen-to-nitrogen ratio, not only are technological requirements of synthetic ammonia satisfied and is stable technological operation guaranteed, but also the net value of ammonia at the outlets of the ammonia synthesis towers and the nitrogen and hydrogen utilization ratios are improved; and besides, each stage of synthesis is performed at low pressure, so that the energy consumption of the ammonia synthesis process is greatly reduced.

Description

technical field [0001] The invention belongs to the technical field of ammonia synthesis, and in particular relates to a segmented ammonia synthesis process. Background technique [0002] Ammonia is one of the important inorganic chemical products and occupies an important position in the national economy. Except that liquid ammonia can be directly used as fertilizer, nitrogen fertilizers used in agriculture, such as urea, ammonium nitrate, ammonium phosphate, ammonium chloride and various nitrogen-containing compound fertilizers, all use ammonia as raw material. Therefore, synthetic ammonia plays an important role in the national economy. The world's annual synthetic ammonia output has reached more than 100 million tons, of which about 80% of ammonia is used to produce chemical fertilizers, and 20% is used as raw materials for other chemical products. [0003] As we all know, synthetic ammonia is directly synthesized by nitrogen and hydrogen under high temperature, high pr...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01C1/04B01J23/652B01J37/02B01J37/18B01J37/08
Inventor 江莉龙林建新倪军林炳裕林科
Owner BEIJING SJ ENVIRONMENTAL PROTECTION & NEW MATERIAL CO LTD
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