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Synchronous heat exchange gas absorption tower and nitric oxide absorption and concentration process

A technology of gas absorption and nitrogen oxides, applied in chemical instruments and methods, separation of dispersed particles, separation methods, etc., can solve problems such as increased power consumption and operating costs, uncontrollable reaction rate, uneven absorption efficiency, etc., to achieve governance Good effect, improved reaction and absorption efficiency, and compact device

Inactive Publication Date: 2011-05-25
NANJING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The patent ZL200610039814.1 authorized by the inventor of this patent proposes a complete set of process for treating and recovering nitrogen oxides, including absorption, bleaching, and concentration processes. This set of process has been used in enterprises producing adipic acid, oxalic acid, and DNT (all adopt Nitric acid is used as an oxidant, and after the gunpowder smoke is absorbed, it becomes high-concentration nitric acid for recycling) successfully applied, but there are still some defects. Increased power consumption and operating costs; on the other hand, since the heat of reaction can only be extracted after the absorption liquid flows through a section of packing, the removal of the heat of reaction is delayed, resulting in a large temperature difference between each section of packing, and the reaction rate is uncontrollable , the absorption efficiency is not uniform, which requires more theoretical stages of absorption to meet the process requirements, making the process longer, usually requiring 2 to 3 absorption towers

Method used

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  • Synchronous heat exchange gas absorption tower and nitric oxide absorption and concentration process
  • Synchronous heat exchange gas absorption tower and nitric oxide absorption and concentration process
  • Synchronous heat exchange gas absorption tower and nitric oxide absorption and concentration process

Examples

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Embodiment 1

[0032] Embodiment 1: adopt 40% nitric acid to make oxidizing agent to produce adipic acid product, produce NO X Exhaust gas, flow rate 5000Nm 3 / h, NO X The average mass concentration of 25%, of which NO and NO 2 About 2:1. The exhaust gas and air are mixed at a volume ratio of 2:1 and then enter the absorption tower, and dilute nitric acid wastewater with a mass concentration of 1.5% is used as an absorbent. The operating pressure of the absorption tower is 4.2atm, and 50 layers of composite bubble-cap trays with heat exchange coils are used inside for absorption. 10 upper trays, 1 row of coils between the tray bubble caps, with a plate spacing of 0.8m; 15 middle trays, 2 rows of coils, with a plate spacing of 0.6m; 25 lower trays, 3 rows of coils, and a plate spacing 0.5m. The diameter of the absorption tower is 2.4m. NO in exhaust gas X The emission concentration is 134ppm, and the rate is 0.78kg / h. Nitric acid with a mass concentration of 40% flows out from the abs...

Embodiment 2

[0033] Implementation example 2: adopt 55% nitric acid to make oxidant to produce methanol catalyst, produce NO and NO 2 Gas, the ratio is about 1:1, the flow rate is 500Nm 3 / h. The operating pressure of the absorption tower is 8atm, and the top adopts 30 layers of composite bubble-cap trays with heat exchange coils for absorption. There are 2 sections of packing at the bottom of the tower, and 350Y-type structured packing is used above 4m, and the height of each tray is 200mm. There is a heat exchange coil; the bottom is filled with a 38mm saddle ring with 2m, and no heat exchange coil is provided. The exhaust gas and air are mixed in a volume ratio of 1:2, and then enter the absorption tower from the middle of the two packings, that is, below the structured packing, and another stream of air (with NO X Gas volume ratio 1:1) enters the absorption tower from the bottom of the tower, that is, below the saddle ring packing, and is used for bleaching high-concentration nitric ...

Embodiment 3

[0034] Implementation Example 3: Adopt 50% nitric acid to make oxidant to produce oxalic acid, produce NO and NO containing 50% 2 Gas, flow rate 1500m 3 / h. The waste gas and air are mixed at a volume ratio of 1:2.5 and then enter the absorption tower. The operating pressure of the absorption tower is 6.8 atm, and the absorbent is clean water. The top adopts 30 layers of composite bubble-cap trays with heat exchange coils for absorption. There is a section of packing at the bottom of the tower, which uses 500Y structured packing of 3m, and the height of each plate is 200mm. There are heat exchange coils between each plate. In the tray section, there are 9 trays in the upper part, 1 row of coils between the bubble caps of the trays, with a plate spacing of 0.5m; 16 trays in the middle, 2 rows of coils, and a plate spacing of 0.45m; 15 lower trays, 3 rows of coils , The board spacing is 0.4m. The diameter of the absorption tower is 1.6m. NO in exhaust gas X The discharge co...

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Abstract

The invention discloses a synchronous heat exchange gas absorption tower, which is a bubble-cap tower. The bottom of the tower is provided with a liquid outlet and a gas inlet; the top of the tower is provided with a tail gas outlet and an absorption liquid outlet; 1 to 3 layers of heat exchange coils are arranged between bubble caps of each layer of tower tray; inlets and outlets of the heat exchange coils are directly communicated with the outside of the tower; and a heat transfer medium flows in the heat exchange coils. The invention also discloses a nitric oxide absorption and concentration process by employing the synchronous heat exchange gas absorption tower. The process comprises the following steps of: mixing a NOX-containing waste gas and air according to the concentration and class of the waste gas in a certain ratio, introducing the mixed gas from the bottom of the absorption tower, introducing water or dilute nitric acid serving as an absorber from the top of the tower, performing countercurrent or crosscurrent contact reaction of the mixed gas and the absorber on each stage of filler or tower plate, timely bringing away reaction heat by using cooling water in the heat exchange coils on each stage of filler and tower plate, ensuring that the NOX concentration in the exhaust tail gas on the top of the absorption tower is 150ppm and the rate is 1kg / h, and obtaining nitric acid with the concentration of 35 to 58 percent at the bottom of the absorption tower.

Description

technical field [0001] The present invention relates to gas absorption tower, and NO X Environmental protection of waste gas. Background technique [0002] Nitrogen oxides (mainly referring to NO and NO 2 , commonly known as NOx) will form yellow or brown smog in the air, commonly known as "yellow dragon", which is one of the important sources of air pollution at present. NO X Exhaust gas will not only cause acid rain and acid fog, but also destroy the ozone layer, causing serious harm to the natural environment and human production and life. Processes such as the nitric acid industry, fuel combustion, and motor vehicle exhaust release large amounts of nitrogen oxides. According to incomplete statistics, in 2005, my country's nitrogen oxide emissions were as high as 22.2 million tons, ranking among the highest in the world. The air pollution and acid rain caused by this are serious, and the economic losses are huge, seriously restricting the sustainability of my country'...

Claims

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Application Information

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IPC IPC(8): B01D53/18
Inventor 耿皎张锋王晓旭袁刚彭璟张志炳
Owner NANJING UNIV
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