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Nitric acid tail gas denitration method

A technology of nitric acid tail gas and process, applied in the field of nitric acid tail gas denitrification process, can solve the problems of uneven local mixing, affect the effect of emission reduction, increase production cost, etc., achieve good emission reduction effect, avoid compression or pressurized steam process, operation low cost effect

Inactive Publication Date: 2019-01-11
SICHUAN GOLDEN ELEPHANT SINCERITY CHEM CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the existing selective catalytic reduction reaction (SCR method) uses gaseous ammonia as a reducing agent, consumes gaseous ammonia as a raw material, and because of the small flow rate of gaseous ammonia, it is prone to local uneven mixing, resulting in local NH 3 The / NOx molar ratio is not appropriate, which directly affects the emission reduction effect and increases the ammonia consumption of the system
In addition, since the pressure levels of the gas ammonia used in the nitric acid plant and the gas ammonia used for emission reduction are inconsistent, additional devices (such as ammonia compressors or pressurized ammonia distillation devices) need to be added to provide higher pressure gas ammonia, resulting in increased production costs

Method used

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Examples

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Effect test

Embodiment 1

[0029]A nitric acid tail gas denitrification process, for the tail gas of the double pressurized dilute nitric acid process, in the case of selecting a medium temperature selective reduction catalyst (commercially available), the initial activity temperature of the selective reduction catalyst is ≥ 200 °C. The installation position of the emission reduction device is at the exhaust pipe section where the exhaust gas preheating temperature reaches 220°C, that is, between the exhaust gas heater 3 and the exhaust gas heater 4, the exhaust gas pressure is 0.6MPa, the exhaust gas temperature is 230°C, and the exhaust gas flow rate is 65,000 3 / h, the NOx content in the design tail gas is 150ppm, the exhaust gas pressure of the synthetic ammonia ammonia tank is 2.1MPa, and the exhaust gas composition is NH 3 : 38%, H 2 : 42%, CH 4 ~8%, N 2 ~12%, the sum of the total volume percentage is 100%.

[0030] The process specifically includes the following steps:

[0031] The first step...

Embodiment 2

[0037] A nitric acid tail gas denitrification process is aimed at the tail gas of the high-pressure dilute nitric acid process. In the case of selecting a high-temperature selective reduction catalyst, the initial activity temperature of the selective reduction catalyst is ≥ 360°C. The installation position of the emission reduction device is before the tail gas is heated and then enters the expander. Usually, the tail gas pipe section with a temperature ≥ 380°C, the tail gas pressure is 0.6MPa, the tail gas temperature is 380°C, and the tail gas flow rate is 45000Nm 3 / h, the NOx content in the design tail gas is 250ppm, the exhaust gas pressure of the synthetic ammonia ammonia tank is 2.1MPa, and the exhaust gas composition is NH 3 : 40%, H 2 : 38%, CH 4 ~8%, N 2 ~14%, the sum of the total volume percentage is 100%.

[0038] The process specifically includes the following steps:

[0039] Step 1: Use the exhaust gas 1 of the synthetic ammonia tank, pass through the remote...

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Abstract

The invention belongs to the technical field of nitric acid production devices and discloses a nitric acid tail gas denitration method. The method comprises: injecting purge gas of an ammonia tank forammonia synthesis as a reducing agent into nitric acid tail gas at a certain temperature (depending on the initial activation temperature of the catalyst), carrying out uniform mixing, feeding the mixture into a denitration reactor, wherein hydrogen reacts with oxygen to form water and gas ammonia decomposes NOx in the exhaust gas into nitrogen gas and water vapor that are environmentally friendly, and discharging the gas into air. The reducing agent is purge gas of the ammonia tank for ammonia synthesis so that the difficulty and energy consumption of the purge gas recovery are reduced and the raw material ammonia use is reduced. The ammonia gas easily reacts with oxygen so that the catalyst can be activated at a lower temperature the selective reaction of ammonia and NOx is easy. The purge gas pressure is higher than the pressure of nitric acid tail gas and is stable so that the compression or pressurized vaporization process required for the use of the gas ammonia is avoided. The whole process reduces an investment, is stable in operation, realizes a low operation cost and has good emission reduction effects.

Description

technical field [0001] The invention belongs to the technical field of nitric acid production devices, in particular to a nitric acid tail gas denitrification process. Background technique [0002] The nitric acid industry in the chemical industry is highly polluting. China has become the world's largest producer of nitric acid, so pollution control and environmental management have also been developed and valued. In the production process of nitric acid, NOx emissions are large, and nitrogen oxides are one of the causes of air pollution. Excessive NOx emissions will inevitably cause environmental damage and harm to human body, so the prevention and control of NOx pollution is very important. [0003] At present, there are many methods to choose from for NOx denitrification of emissions after the production of nitric acid, but considering many factors such as simple operation, stable effect, long service life, cost, energy saving, etc., it is difficult to use selective ca...

Claims

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Application Information

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IPC IPC(8): B01D53/56B01D53/74B01D53/86
CPCB01D53/56B01D53/74B01D53/8628B01D2251/2062
Inventor 王明权余波
Owner SICHUAN GOLDEN ELEPHANT SINCERITY CHEM CO LTD
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