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Cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst for diesel engine

A technology of binary oxides and supported catalysts, applied in the direction of metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical/physical processes, etc., can solve the catalytic performance of unfavorable supported catalysts for low-temperature SCR reactions , poor low temperature activity, poor oxygen storage performance and other problems, to improve the catalytic performance of low temperature SCR reaction, reduce the harm to the environment and human health, and enhance the effect of oxygen storage performance

Active Publication Date: 2017-06-06
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, V as the main active ingredient 2 o 5 It is a highly toxic substance, and its loss during the use of the SCR system will inevitably endanger environmental safety
At the same time, as one of the coating materials, TiO 2 The cost is high, and its own oxygen storage performance is not good, which is not conducive to the further improvement of the catalytic performance of the low-temperature SCR reaction of the supported catalyst
The characteristic of vanadium-based SCR catalyst is that it has good NOx purification performance after the exhaust temperature exceeds 280°C, but its low-temperature activity is not good, and it is difficult to adapt to the operation of diesel vehicles under the conditions of congested roads, slow speed, and low exhaust temperature.

Method used

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  • Cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst for diesel engine
  • Cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst for diesel engine
  • Cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst for diesel engine

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] (1) Determination of the amount of catalyst raw material used

[0031] The design requires the preparation of Co in the main active component of the catalyst 2 o 3 and V 2 o 5 The mass ratio is: 66.7%: 33.3%; the mass ratio of the main active ingredient, co-catalyst and coating additive is: 3%: 9%: 88%; in the coating additive, CeO 2 , ZrO 2 , γ-Al 2 o 3 and anatase TiO 2 The mass ratio is: 20%:10%:20%:50%; pure γ-Al in coating additives 2 o 3 Transformation of powder and aluminum sol to generate γ-Al 2 o 3 The mass ratio of the coating is: 50%:50%; the mass ratio of the coating to the carrier is 20%:80%. The planned 400-mesh cordierite honeycomb ceramic carrier to be coated is 800g, based on which the content of various components in the cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst can be calculated: Co 2 o 3 4g, V 2 o 5 2g, WO 3 18g, CeO 2 35.2g, ZrO 2 17.6g, pure γ-Al 2 o 3 γ-Al converted from powder 17.6g...

Embodiment 2

[0039] (1) Determination of the amount of catalyst raw material used

[0040] The design requires the preparation of Co in the main active component of the catalyst 2 o 3 and V 2 o 5 The mass ratio is: 50%:50%; the mass ratio of the main active ingredient, co-catalyst and coating aid is: 2%:5%:93%; in the coating aid, CeO 2 , ZrO 2 , γ-Al 2 o 3 and anatase TiO 2 The mass ratio is: 30%:0%:30%:40%; pure γ-Al in coating additives 2 o 3 Transformation of powder and aluminum sol to generate γ-Al 2 o 3 The mass ratio of the coating is: 50%:50%; the mass ratio of the coating to the carrier is 30%:70%. The planned 400-mesh cordierite honeycomb ceramic carrier to be coated is 700g, based on which the content of various components in the cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst can be calculated: Co 2 o 3 3g, V 2 o 5 3g, WO 3 15g, CeO 2 83.7g, pure γ-Al 2 o 3 Powder 41.85g, γ-Al converted from aluminum sol 2 o 3 41.85g ...

Embodiment 3

[0048] (1) Determination of the amount of catalyst raw material used

[0049] The design requires the preparation of Co in the main active component of the catalyst 2 o 3 and V 2 o 5 The mass ratio is: 50%: 50%; the mass ratio of the main active ingredient, cocatalyst and coating aid is: 8%: 20%: 72%; in the coating aid, CeO 2 , ZrO 2 , γ-Al 2 o 3 and anatase TiO 2 The mass ratio is: 30%:0%:50%:20%; pure γ-Al in coating additives 2 o 3 Transformation of powder and aluminum sol to generate γ-Al 2 o 3 The mass ratio is: 50%:50%; the mass ratio of the coating to the carrier is 10%:90%. The planned 400-mesh cordierite honeycomb ceramic carrier to be coated is 900g, based on which the content of various components in the cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst can be calculated: Co 2 o 3 4g, V 2 o 5 4g, WO 3 20g, CeO 2 21.6g, pure γ-Al 2 o 3 Powder 18g, γ-Al converted from aluminum sol 2 o 3 18g and anatase TiO 2...

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PUM

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Abstract

The invention discloses a cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst for a diesel engine. According to the catalyst, the cobalt-vanadium binary oxide is taken as a main active component, WO3 is taken as a cocatalyst, CeO2, ZrO2, gamma-Al2O3 and anatase type TiO2 are combined to form coating auxiliaries, and 400-mesh cordierite honeycomb ceramics are taken as a supported catalyst carrier. The preparation process of the cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst comprises the following steps: determining the usage amounts of the catalyst raw materials, preparing a coating slurry precursor and a coating slurry, and applying the coating slurry. A urea solution or ammonia gas is taken as a reducing agent for the catalyst. According to the cobalt-vanadium binary oxide type selective catalytic reduction supported catalyst for the diesel engine, low-toxicity Co2O3 is adopted to take the place of high-toxicity V2O5, so that the damage caused by the catalyst is reduced and the low-temperature selective catalytic reduction (SCR) reaction catalytic activity of the catalyst is improved. Cerium oxide and zirconium oxide are added to the coating to enhance the oxygen storage capacity of the catalyst; the alumina sol is taken as a coating binder, so that the raw material cost and process difficulty of catalyst production are reduced.

Description

technical field [0001] The invention belongs to diesel engine tail gas purification technology, in particular to a catalyst used for automobile tail gas purification and a preparation method thereof. Background technique [0002] With the rapid growth of global motor vehicle production, automobile exhaust has become the nitrogen oxide (NO X ) is one of the most important sources. NOx is not only a toxic and irritating substance, but also a precursor of secondary ultrafine particles and acid rain, which seriously endangers the atmospheric environment and human health. As one of the main driving forces of motor vehicles, diesel engines not only have high specific NOx emissions, but also because the single engine power of diesel engines is generally higher than that of gasoline engines, the NOx emissions of diesel vehicles are much higher than those of gasoline vehicles. In addition, since the diesel engine adopts a lean-burn, oxygen-enriched combustion method, the exhaust ga...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/888B01D53/56B01D53/94
CPCY02T10/12
Inventor 宋崇林吕刚宋金瓯张清茂
Owner TIANJIN UNIV
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