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Catalysed filter system for treating particulate-containing exhaust gas from stationary emission sources

A catalytic filtration and emission source technology, applied in the direction of dispersed particle filtration, exhaust equipment, gas treatment, etc., can solve the problems of not so high mechanical strength, increase filter porosity, reduce filter mechanical strength, etc.

Pending Publication Date: 2021-09-28
JOHNSON MATTHEY PLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, increasing filter porosity also reduces the mechanical strength of the underlying filter
Third, this arrangement also reduces the mechanical strength of the filter for catalysts disposed in the base wall of the filter
[0021] Consequently, design options become more limited due to the incorporation of specific catalysts within the filter walls, e.g., a specific binder is required for desired catalyst activity, but is not compatible with using an alternative binder that does not provide the desired catalytic function. This may result in products with less mechanical strength compared to

Method used

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  • Catalysed filter system for treating particulate-containing exhaust gas from stationary emission sources
  • Catalysed filter system for treating particulate-containing exhaust gas from stationary emission sources
  • Catalysed filter system for treating particulate-containing exhaust gas from stationary emission sources

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0083] Example 1 - Procedure for Candle Filter Insert Synthesis

[0084] While stirring, mix enough 3 The commercially available TiO 2 The powder was added to the water in the blender so that the final weight fraction of solids was 30%.

[0085] The resulting slurry was ball milled to reduce the particle size to d50<6 μm.

[0086] After grinding, the slurry was returned to the mixer.

[0087] Mix the vanadyl oxalate into the slurry. Add NH if necessary 3 To maintain the pH between 6.5-7.5, thereby controlling the rheological properties of the washcoat.

[0088] The silica sol was added to the slurry while mixing. The pH was again maintained between 6.5-7.5.

[0089] The resulting slurry (now referred to as washcoat) is diluted to the appropriate solids content for washcoating. Adjust pH as needed to maintain between 6.5-7.5

[0090] The washcoat is poured into a pan of sufficient size to allow the fiberglass mat to dip into it.

[0091] Dip the fiberglass mat into ...

Embodiment 2

[0096] Example 2 - Preparation of Oxidation Catalyst Catalyzed Glass Mats

[0097] The method is similar to that used in Example 1. Mix enough γ-Al 2 o 3 Added to water to achieve 50 wt% Al 2 o 3 solid concentration. The alumina slurry batch in water was transferred to a ball mill and ground to a particle size below 15 μm (D50 about 4 μm and D90 about 8 μm) while maintaining the pH 2 o 3 . Tetraaminoplatinum nitrate was added to the slurry. The pH was controlled at pH 6 using ammonium nitrate or acetic acid.

[0098] Dip a fiberglass mat into the resulting washcoat and place on a drying rack to drip dry.

[0099] The catalyzed glass fiber mat was dried in an oven at 80°C in air, followed by firing at 525°C to activate the catalyst.

Embodiment 3

[0100] Example 3 - Testing of SCR Catalyst Catalyzed Glass Fiber Mat Inserts in Candle Filters

[0101] A 9 inch by 25 inch section of the SCR catalytic glass fiber mat prepared according to Example 1 was rolled into a tube, ie a tube including a hollow portion therein, and one end was folded over itself to prevent gas bypass during the test. The rolled tube is then inserted into a bare uncatalyzed low alkali circular cross-section candle filter approximately 8 inches long, with the folded end of the tube inserted first so that the folded end is aligned with the closed end of the candle filter Apposition. At temperatures in the range of 250°C to 450°C, at Figure 6A In the Adapted Synthetic Catalytic Activity Test (SCAT) apparatus 10 shown, a candle filter comprising a fiber mat insert catalyzed by an SCR catalyst was tested for SCR activity. The candle filter 12 to be tested is mounted hermetically (using appropriate gaskets (not shown) and four equidistant nut and bolt f...

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Abstract

The invention relates to a catalysed filter system for treating particulate-containing exhaust gas from a stationary emission source. The catalysed filter system for treating particulate-containing exhaust gas from a stationary emission source comprises an elongate filter element comprising porous walls which define a hollow section and a substrate material supporting a catalyst component disposed within the hollow section, the arrangement being such that gas entering the hollow section of the elongate filter element from across the porous walls thereof must contact the substrate material supporting the catalyst component before exiting the hollow section of the elongate filter element.

Description

technical field [0001] The present invention relates to a catalytic filter system for the treatment of particulate-laden exhaust gases from stationary sources such as cement or glass manufacturing or coal, biomass or heavy fuel oil power generation comprising elongated filter elements , the elongate filter element comprising a porous wall defining a hollow portion. The elongate filter element may be, for example, a candle filter. Background technique [0002] There are many methods in which a hot gaseous medium containing particulate matter is produced which must be separated from the gaseous medium to prevent contamination, or to remove hazardous substances. High temperature filtration of particles has become an important component in many emerging technologies. For example, advanced coal conversion technologies, such as fluidized bed gasification and combustion, depend on the successful removal of particulates at temperatures in the range of about 500°C to 1000°C. Other...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D46/02B01D46/24B01D53/86B01D53/88B01D46/00
CPCB01D46/2407B01D46/023B01D53/8631B01D53/885B01D46/2411B01D46/0027B01D46/521B01D2257/404B01D2255/102B01D2255/104B01D2255/106B01D2255/20746B01D2255/2073B01D2255/20753B01D2255/20761B01D2255/20738B01D2255/20723B01D2255/20769B01D2255/20776Y02C20/10B01D46/64B01D2258/0233B01D2258/0241B01D2258/0291F01N3/0212F01N3/035F01N3/2066F01N2590/10B01D53/9418B01D46/2422B01D53/56B01D53/9427F01N2250/02F01N2330/00F01N13/017F01N2450/30
Inventor P·J·安德森T·M·叶
Owner JOHNSON MATTHEY PLC