Low-consumption and low-emission nitric acid production method and production equipment thereof

A production method and technology of production equipment, applied in the field of methods and production equipment, can solve the problems of not reaching 300 mg/Nm, achieve the effects of increasing oxidation speed, reducing consumption, and compact process flow

Inactive Publication Date: 2012-06-13
CHINA CHENGDA ENG
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  • Abstract
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  • Application Information

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Problems solved by technology

[0004] (2), the nitrogen oxides emitted from the tail gas are 400mg / Nm 3 , not reaching the national 300 mg / Nm 3 , emission index;

Method used

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  • Low-consumption and low-emission nitric acid production method and production equipment thereof
  • Low-consumption and low-emission nitric acid production method and production equipment thereof

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Embodiment Construction

[0026] Below in conjunction with accompanying drawing, the present invention is described in detail.

[0027] In order to make the object, technical solution and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.

[0028] Such as figure 1 As shown, a low-consumption, low-emission nitric acid production equipment includes an oxidation reactor 1, a heat exchanger 5, a water cooler 6 and a nitric acid absorption tower 7 connected in sequence, and platinum is arranged in the oxidation reactor 1. Catalyst layer 2 and waste heat boiler 4, the air inlet of the oxidation reactor 1 is communicated with the air compressor 9 and the ammonia gas pipeline through pipelines, and the tail gas discharge port at the top of ...

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Abstract

The invention discloses a low-consumption and low-emission nitric acid production method and production equipment thereof. The method and the equipment adopts the same low-pressure level for oxidation and absorption, the double-pressurization high-pressure level is omitted, a molecular sieve absorption device is adopted for tail gas treatment of a nitric acid absorption tower, in addition, secondary air is used for taking reaction with nitric oxide absorbed in the molecular sieve absorption device to form regenerated gas, the regenerated gas is sent into the nitric acid absorption tower to be recovered and reutilized, the nitrogen oxide content in the tail gas is lower than 100mg / Nm<3>, in addition, the yield of the nitric acid can also be improved through the recovery and the utilization of regeneration gas, a layer of silk screen is arranged on a sieve plate tower disc of an oxidation section of the nitric acid absorption tower, the oxidation speed at high pressure and low pressure can be effectively accelerated, and an N20 decomposition catalyst layer is also additionally arranged in an oxidation reaction vessel, so the N20 content in the nitric oxide gas in the oxidation reaction vessel can be reduced to about 100PPM. The nitric acid production method does not need to adopt two pressure levels, no nitric oxide compressor is adopted, no tail gas ammonification re-treatment device is adopted, the investment is greatly saved, and the consumption is reduced.

Description

technical field [0001] The invention relates to the technical field of producing nitric acid, in particular to a method for producing nitric acid by using ammonia and air and production equipment thereof. Background technique [0002] At present, the new processes of producing nitric acid with ammonia and air at home and abroad include normal pressure method (that is, the oxidation pressure and absorption pressure are normal pressure), medium pressure method (that is, the oxidation pressure and absorption pressure are 0.3 to 0.4 Mpa) and high pressure method (that is, The oxidation pressure and absorption pressure are 1.0 to 1.2 Mpa,), while the most advanced nitric acid production process belongs to the double pressure method, that is, the oxidation pressure is 0.4 to 0.5 Mpa, and the absorption pressure is 1.0 to 1.2 Mpa, which can make the oxidation The consumption of platinum is lower, and the purpose of nitrogen oxides in tailpipe emissions is also lower. The main prob...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B21/38
CPCY02P20/129
Inventor 曾纪龙熊兴和许斌王时川梁万才
Owner CHINA CHENGDA ENG
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