Modified catalyst for gaseous-state elemental mercury oxidation and preparation method of modified catalyst

A catalyst and elemental mercury technology, which is applied in the direction of physical/chemical process catalysts, chemical instruments and methods, separation methods, etc., can solve the problems of catalytic oxidation rate less than 15%, expensive, difficult to apply, etc., to achieve sustainable development, Long-lasting, low-cost effects

Active Publication Date: 2013-03-13
KUNMING METALLURGY INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented process uses special materials that help remove harmful elements like arsine (AsH3) from exhaust gases effectively without causing pollution or damaging equipment overtime.

Problems solved by technology

This patented describes various methods used during combustible material production processes like coal burning plants where harmful substances called mercuric compounds were released into air over time. These contaminating agents could cause serious hazards if they remain untreated within certain periods after being produced. To address this issue, there has been developed an improved method for controlling these materials through specific types of catalysis techniques.

Method used

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  • Modified catalyst for gaseous-state elemental mercury oxidation and preparation method of modified catalyst
  • Modified catalyst for gaseous-state elemental mercury oxidation and preparation method of modified catalyst
  • Modified catalyst for gaseous-state elemental mercury oxidation and preparation method of modified catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Example 1 Anhydrous MnCl 2 Add in deionized water, stir evenly, and prepare different MnCl 2 Mass fraction of impregnation solution (MnCl 2 The solubility in water is shown in Table 1), and then the dried γ-Al 2 o 3 The pellets were respectively immersed in the above solution, stirred slightly and dipped for 6 h, dried at 80 °C for 8 h, heated at 200 °C for 2 h under nitrogen purging, and then heated at 380 °C for 3 h under nitrogen purging to prepare Catalyst MnCl with different content of catalytic components 2 / γ-Al 2 o 3 . Different MnCl 2 The mass fraction of each catalyst prepared by impregnating solution vs. Hg 0 The catalytic oxidation efficiency is shown in Table 2.

[0029] Table 1 MnCl 2 Solubility in water

[0030]

[0031] Table 2 Catalytic oxidation efficiency of catalyst

[0032]

Embodiment 2

[0033] Example 2 with anhydrous MnCl 2 As a catalytic component, (NH 4 ) 6 Mo 7 o 24 4H 2 O is used as a doping modification component, and (NH 4 ) 6 Mo 7 o 24 4H 2 O and MnCl 2 Mix according to different molar ratios, add deionized water and stir evenly to obtain MnCl-containing 2 The impregnation solution with a mass fraction of 15%, and then the dried γ-Al 2 o 3 The carrier pellets were respectively immersed in the above solution, stirred slightly and immersed for 6 h, then dried at 80 °C for 8 h, heated at 200 °C for 2 h under nitrogen purging, and then heated at 380 °C for 3 h under nitrogen purging. Catalyst MoO with different content of doped modification components and catalytic components prepared 3 -MnCl 2 / γ-Al 2 o 3 . (NH 4 ) 6 Mo 7 o 24 4H 2 O and MnCl 2 The effect of each catalyst on Hg prepared by impregnating solution mixed in different molar ratios 0 The catalytic oxidation efficiency is shown in Table 3.

[0034] Table 3 Catalytic oxid

Embodiment 3

[0036] Example 3 (NH 4 ) 6 Mo 7 o 24 4H 2 O and MnCl 2 Mix at 0.5% by mole ratio, add deionized water and stir evenly to obtain 2 and (NH 4 ) 6 Mo 7 o 24 The soaking liquid of mass fraction, all the other are identical with embodiment 2. Different MnCl 2 and (NH 4 ) 6 Mo 7 o 24 The mass fraction of each catalyst prepared by impregnating solution vs. Hg 0 The catalytic oxidation efficiency is shown in Table 4.

[0037] Table 4 Catalytic oxidation efficiency of modified catalysts

[0038]

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Abstract

The invention provides a modified catalyst for gaseous-state elemental mercury oxidation and a preparation method of the modified catalyst, belonging to the technical field of mercury removal from smoke. The catalyst is the modified catalyst formed by loading a catalysis component manganese chloride, and a doping modification component ammonium molybdate on a catalytic carrier, wherein the total load of molybdenum, manganese and chlorine is 1.25-25 wt%, and the molar ratio of the three elements is (0.007-0.14): 1: 2. Experimental results indicate that via the preparation method, the three elements molybdenum, manganese and chlorine can be uniformly dispersed on the catalytic carrier to inhibit the grain agglomeration of the catalyst during the preparation process and form a more stable aggregate, thus effectively increasing the efficiency of oxidation for gaseous-state HgO; and the catalyst is very strong in catalytic oxidation performance and sulphur-resistant performance for the gaseous-state HgO in a temperature ranging from 100 to 200 DEG C, and long in endurance time; and the catalytic oxidation efficiency of converting the gaseous-state HgO to Hg<2+> is greater than 97%.

Description

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Claims

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Application Information

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Owner KUNMING METALLURGY INST
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