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A process for recovery and treatment of tail gas from synthetic ammonia

A tail gas recovery and treatment process technology, applied in the field of ammonia synthesis, can solve the problems that the tail gas of synthesis ammonia cannot be optimally utilized, waste of resources, and no treatment plan, etc.

Active Publication Date: 2017-07-07
新疆宜化化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

It is very uneconomical to burn hydrogen and the like as fuel, so it has always been a hot spot for those skilled in the art to extract the valuable components in the purge gas; Correspondingly, the tail gas of synthetic ammonia in the prior art cannot be optimally utilized, resulting in a waste of resources to a certain extent

Method used

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Embodiment Construction

[0034] In order to make the object, technical solution and advantages of the present invention more clear, the embodiments of the present invention will be described in detail below. It should be noted that, in the case of no conflict, the embodiments in the present application and the features in the embodiments can be combined arbitrarily with each other.

[0035] The invention provides a process for recovering and treating tail gas from synthetic ammonia, which may include:

[0036] Step a: Raw gas compression operation,

[0037] The ammonia recovery tail gas is sent to the compressor to complete the raw gas compression operation, and when the raw gas is pressurized to 4.2MPa, the raw gas is output from the compressor;

[0038] Step b: raw material gas cooling operation,

[0039] Send the raw gas output from the compressor to the cooler for raw gas cooling operation, and when the raw gas is cooled to normal temperature, output the raw gas from the cooler;

[0040] Step c...

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PUM

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Abstract

The invention discloses a tail gas recovery and treatment process for synthetic ammonia, which includes: step a: raw material gas compression operation, transporting the tail gas recovered from ammonia to a compressor to complete the raw material gas compression operation, and when the pressure is increased to 4.2MPa, the raw material gas is compressed machine output; step b: raw material gas cooling operation, the raw material gas output from the compressor is transported to the cooler for raw material gas cooling operation, and when cooled to normal temperature, the raw material gas is output from the cooler; step c: raw material gas washing operation, The raw material gas output from the cooler is transported to the water washing tower for water washing operation of the raw material gas. When the ammonia is separated to below 100PPm, the raw material gas is output from the water washing tower and other operations. The present invention can be applied to the technical field of synthetic ammonia, and the synthetic ammonia can be converted Tail gas is recovered to the greatest extent, and the largest part of LNG products and nitrogen and hydrogen are obtained; it can ensure that the concentration of liquid methane output from the bottom of the methane distillation tower is above 99.5%.

Description

technical field [0001] The invention relates to the technical field of synthetic ammonia, in particular to a recovery and treatment process for synthetic ammonia tail gas. Background technique [0002] In the existing technology, synthetic ammonia is the foundation of the chemical industry and the pioneer of the development of my country's chemical industry. After decades of development, my country's synthetic ammonia industry has been greatly improved in terms of industrial scale, domestic self-sufficiency, and technical equipment level. At present, the scale of my country's synthetic ammonia industry ranks first in the world, accounting for about one-third of the world's total. Synthetic ammonia, as an important basis for the industrial production of chemical fertilizers, plays an important role in my country's national economy. Due to the development process of small nitrogen fertilizer, medium nitrogen fertilizer and large nitrogen fertilizer in history, the number of s...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B3/50C01B21/04C01B23/00C07C9/04C07C7/04
Inventor 张书培张忠华汪万新朱洪波吴世华汪建国时兴亚尹学文陶建彬
Owner 新疆宜化化工有限公司