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Online activation method of catalytic oxidation VOCs catalyst

A catalytic oxidation and activation method technology, applied in catalyst regeneration/reactivation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of high price, shortened catalyst service life and heavy operation burden and other problems, to achieve the effect of reducing operating costs, reducing catalyst consumption, and reducing workload

Pending Publication Date: 2019-12-13
LIVE FRESH INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The effective active components of catalysts used for VOCs treatment are mainly precious metals such as platinum, palladium, rhodium, etc., and most of them are imported and expensive
The cost of the catalyst accounts for more than 1 / 2 of the operating cost of the entire VOCs treatment project. If the service life of the catalyst is greatly shortened due to deactivation, it will be a lot of money to replace the new catalyst. In addition, the cost of hazardous waste disposal of the waste catalyst, For environmental protection facilities that generate little or no economic benefits, it further increases the burden on corporate operations

Method used

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  • Online activation method of catalytic oxidation VOCs catalyst
  • Online activation method of catalytic oxidation VOCs catalyst
  • Online activation method of catalytic oxidation VOCs catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] A and B groups of deactivated catalyst samples are all from the VOCs exhaust gas catalytic oxidation treatment equipment in operation in a certain factory. Due to improper on-site operation, the catalyst was deactivated by moisture. The distribution ratio of active components of group A catalyst is silver: manganese: cerium = 1:3:4, the distribution ratio of active components of group B catalyst is silver: manganese: cerium = 0.25:1.5:2, wherein the total ratio of active components of group B Group A is low. Use the activation replenishment solution A potion with the same distribution ratio of the active components of the catalyst in group A (the distribution ratio of the active components is silver: manganese: cerium = 1:3:4) to activate the deactivated catalysts of the two groups A and B online. It can be seen that group A belongs to moderate amount of active ingredient supplementation, and group B belongs to excessive amount of active ingredient supplementation. Spr...

Embodiment 2

[0045] The above-mentioned deactivated group A catalysts are further subdivided into two groups of A1 and A2, and the A1 group is activated by using the activation replenishment liquid A liquid medicine (the active component distribution ratio is silver: manganese: cerium=1:3:4), and the A2 group is activated. The group was activated with the activation replenishment solution B potion (the distribution ratio of the active components was silver: manganese: cerium = 0.25:1.5:2, and the total amount of active components of the B potion was lower than that of the A potion). Active ingredients, group A2 belongs to insufficient supplementary active ingredients. Spray the potion and let it stand overnight, then introduce hot air at 80°C at a space velocity of 5000-10000h -1 Under certain conditions, dry for 4 hours, and then introduce hot air at 250°C at a space velocity of 3000-7000 hours -1 Calcined under the conditions for 4h, the activation regeneration is over. The catalysts o...

Embodiment 3

[0049] The catalyst sample comes from a petrochemical plant that has been running for about one year on the exhaust gas catalytic oxidation treatment equipment. Due to the change of the loading conditions of the plant, propane has been added to the exhaust gas, and the catalytic oxidation effect of the catalyst on propane is not good. It is divided into two groups C and D, and the active components of the catalyst are manganese, cerium and silver. Both groups of catalysts are now sprayed with potion E for on-line activation, wherein the active component of potion E is cobalt with a content of 0.1 to 15 wt%, and does not contain manganese, cerium and silver as active components of deactivated catalysts. The spray flow rate is 45mL / min, and the spray volume is 30% of the weight of the catalyst carrier. After spraying, let it stand overnight, and introduce hot air at 80°C at a space velocity of 5000-10000h -1 Under certain conditions, dry for 4 hours, and then introduce hot air a...

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Abstract

The invention discloses an online activation method of a catalytic oxidation VOCs catalyst. The method comprises the following steps: 1, purging: purging a deactivated catalyst with 200-300 DEG C hotair for 2-3 h to remove oil stains and dusts adsorbed on the catalyst; 2, spraying: naturally cooling the catalyst to normal temperature after the purging is completed, spraying an activation supplementing solution on the catalyst at a speed of 15-60 mL / min, standing overnight to make sprayed active components fully permeate into catalyst holes and the interior of the catalyst, wherein the spraying amount is 30-60% of the weight of a catalyst carrier; and 3, calcining: calcining the catalyst, sprayed with the activation supplementing solution, with the 200-300 DEG C hot air for 1-5 h at an airspeed of 3000-7000 h<-1> in order to finish online activation of the deactivated catalyst. The online activation method of the catalytic oxidation VOCs catalyst makes the performance of the activatedcatalyst recovered to 90% or above of the performance of a fresh catalyst product, prolongs the service life of the catalyst by 1-1.5 years, reduces the loss of the catalyst, and reduces the operation cost of the catalyst by 1 / 3 to 1 / 2.

Description

technical field [0001] The invention relates to the technical field of VOCs catalysts, in particular to an online activation method for catalytic oxidation of VOCs catalysts. Background technique [0002] Globally, natural sources of volatile organic compounds (VOCs) emissions are much higher than man-made sources, but in some industrial-intensive areas of my country, man-made sources of VOCs emissions are much higher than natural sources. In recent years, my country's total VOCs emissions have increased year by year. Chen Ying et al. used the emission factor method to estimate that my country's industrial VOCs emissions in 2009 were about 12 million tons. According to the average annual growth rate of 11.5%, the current total annual VOCs emissions in my country have far exceeded 20 million tons. VOCs emissions are large and harmful, not only directly endangering human health, but also photochemically react with nitrogen oxides under certain meteorological conditions, causi...

Claims

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Application Information

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IPC IPC(8): B01J38/48B01J38/12B01J38/02B01J23/96B01J23/89B01J23/68
CPCB01J38/12B01J38/02B01J38/485B01J23/96B01J23/688B01J23/8986
Inventor 赖庆智敬丹丹龙志颜翔
Owner LIVE FRESH INC
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