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Method for treating non-ferrous metal smelting smoke acid-making tail gas by low-temperature catalytic oxidation cooperated with ultraviolet light

A low-temperature catalysis and oxidation treatment technology, applied in the environmental field, can solve the problems of high one-time investment and operation cost, complex process and large floor space, and achieve the effects of low cost, simple process and low energy consumption.

Inactive Publication Date: 2019-05-17
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, most of the current methods use independent solutions to combine SO 2 , NO x and Hg 0 It is efficiently removed in their respective treatment systems, but this brings an obvious disadvantage that each system is independent of each other, the whole process is complicated, the floor area is large, and the one-time investment and operation costs are high, which brings great harm to the non-ferrous metal smelting industry. great economic pressure

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Removal of SO from non-ferrous metal smelting flue gas acid production tail gas by ultraviolet light synergistic low-temperature catalytic oxidation 2 , NO x , the method of zero-valent Hg, specifically comprise the following steps: the oxygen that feeds in the tail gas of making acid, makes O in the tail gas 2 The volume percentage of the tail gas is 2% of the total tail gas. The tail gas is irradiated with ultraviolet lamps to ionize the oxygen molecules in the oxygen in the tail gas and recombine to generate strong oxidant ozone. Oxidation, solid phase catalytic oxidant layer bed is equipped with solid catalyst, the solid catalyst is made of Al 2 o 3 As the carrier, the active components are manganese and molybdenum, and the mass percentage of the active components in the catalyst is 4%; the temperature of the catalytic reaction bed is 100 °C, and this method is effective for SO in the tail gas 2 , NO x The oxidation efficiencies of zero-valent Hg were 85%, 87%, ...

Embodiment 2

[0017] Removal of SO from non-ferrous metal smelting flue gas acid production tail gas by ultraviolet light synergistic low-temperature catalytic oxidation 2 , NO x , the method of zero-valent Hg, specifically comprise the following steps: the oxygen that feeds in the tail gas of making acid, makes O in the tail gas 2 The volume percentage of the tail gas is 4% of the total tail gas. The tail gas is irradiated with an ultraviolet lamp to ionize the oxygen molecules in the oxygen in the tail gas and recombine to produce a strong oxidant ozone, and then the tail gas is oxidized through the solid-phase catalytic oxidant layer bed; the solid-phase The catalytic oxidant layer bed is equipped with a solid catalyst, which is made of Al 2 o 3 As the carrier, the active components are manganese and molybdenum, and the mass percentage of the active components in the catalyst is 8%; the temperature of the catalytic reaction bed is 250 °C, and this method can reduce 2 , NO x The oxida...

Embodiment 3

[0019] Removal of SO from non-ferrous metal smelting flue gas acid production tail gas by ultraviolet light synergistic low-temperature catalytic oxidation 2 , NO x , the method of zero-valent Hg, specifically comprise the following steps: the oxygen that feeds in the tail gas of making acid, makes O in the tail gas 2 The volume percentage of the tail gas is 6% of the total tail gas. The tail gas is irradiated with an ultraviolet lamp to ionize the oxygen molecules in the oxygen in the tail gas and recombine to produce a strong oxidant ozone. Oxidation, solid phase catalytic oxidant layer bed is equipped with solid catalyst, the solid catalyst is made of Al 2 o 3 As the carrier, the active components are manganese and molybdenum, and the mass percentage of the active components in the catalyst is 5%; the temperature of the catalytic reaction bed is 120 °C, and this method is effective for SO in the tail gas 2 , NO x The oxidation efficiencies of zero-valent Hg were 87%, 91...

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Abstract

The invention discloses a method for treating non-ferrous metal smelting smoke acid-making tail gas by low-temperature catalytic oxidation cooperated with ultraviolet light, and belongs to the technical field of environment. The method for treating the non-ferrous metal smelting smoke acid-making tail gas by the low-temperature catalytic oxidation cooperated with the ultraviolet light comprises the steps that an ultraviolet lamp is used for shining the tail gas, so that oxygen molecules in oxygen in the tail gas generates ionization, recombination is carried out to generate strong oxidant ozone, and the volume percent of O<2> is 2-6% of tail gas total quantity; the tail gas is oxidized through a solid phase catalytic oxidizing agent bed layer after shined by the ultraviolet lamp, and simultaneous desorption of SO<2>, NO<x> and Hg<0> in the acid-making tail gas is realized; the reaction temperature in a catalytic bed is 50-250 DEG C; and a solid catalyst in the solid phase catalytic oxidation process takes aluminum oxide as a carrier, and active components are one or multiple any combination of manganese, molybdenum, cobalt, cerium, iron and copper. According to the method for treating the non-ferrous metal smelting smoke acid-making tail gas by the low-temperature catalytic oxidation cooperated with the ultraviolet light, the removal efficiency of SO<2>, NO<x> and Hg<0> in theacid-making tail gas can reach more than 85%, and cooperative and efficient purification of SO<2>, NO<x> and Hg<0> in a same system in the low-temperature condition is realized.

Description

technical field [0001] The invention relates to a method for treating non-ferrous metal smelting flue gas acid production tail gas by ultraviolet light synergistic low-temperature catalytic oxidation, which belongs to the field of environmental technology. Background technique [0002] Non-ferrous metal smelting mostly uses sulfide concentrates as raw materials, and is a pyrometallurgy process under high temperature and high oxygen conditions, so high concentrations of sulfur dioxide (SO 2 ), and its concentration can be as high as 7%~13%. For most non-ferrous metal smelters, the contact method is usually used to convert high-concentration SO 2 Converted to sulfuric acid, the process is now mature. However, there is still a small amount of SO in the tail gas after acid production 2 , while nitrogen oxides (NO x ) may exist in the flue gas at the outlet of the smelting furnace. During the subsequent acid production process, part of it will enter the finished acid to form n...

Claims

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Application Information

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IPC IPC(8): B01D53/86B01J23/34B01J23/72B01J23/745B01J37/02B01J37/08B01D53/60B01D53/64
CPCY02A50/20
Inventor 李凯赵珂宁平孙鑫王驰宋辛李丁莉秦媛
Owner KUNMING UNIV OF SCI & TECH
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