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Method for regenerating carbonyl sulfide hydrolysis catalyst after inactivation

A hydrolysis catalyst, carbonyl sulfide technology, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of insignificant adsorption of COS, incomplete use of catalysts, etc., achieving low cost, energy saving, The effect of low roasting temperature

Inactive Publication Date: 2013-04-10
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0007] In order to overcome the problems of incomplete use of the catalyst and inconspicuous adsorption of COS, the object of the present invention is to provide a regeneration method after deactivation of the carbonyl sulfide hydrolysis catalyst, so that the deactivation of the carbonyl sulfide hydrolysis catalyst can be regenerated and prolong its service life , saving resources, achieved through the following technical solutions

Method used

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  • Method for regenerating carbonyl sulfide hydrolysis catalyst after inactivation
  • Method for regenerating carbonyl sulfide hydrolysis catalyst after inactivation
  • Method for regenerating carbonyl sulfide hydrolysis catalyst after inactivation

Examples

Experimental program
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Effect test

Embodiment 1

[0033] A. Wash 2 g of the deactivated catalyst with distilled water for 20 minutes on a conventional ultrasonic instrument at a temperature of 30°C and a frequency of 40KHz, and then dry it at 60°C for 12 hours;

[0034] B. Under the same ultrasonic-assisted conditions as above, the catalyst after step A was impregnated with an impregnating solution for 40 minutes, and then dried at a temperature of 70°C for 11 hours. The impregnating solution was a mixture of 7 g of NaOH and 5.2995 g of Na 2 CO 3 The solution obtained by being dissolved in 50ml of water;

[0035] C. Place the catalyst obtained in step B in a muffle furnace, roast it for 2 hours at 350°C, and control the temperature rise rate to 5°C / min to obtain a regenerated catalyst, whose activity is shown in figure 1 .

Embodiment 2

[0037] A. Wash 2 g of the deactivated catalyst with distilled water for 30 minutes on a conventional ultrasonic instrument with the aid of ultrasonic waves at a temperature of 30°C and a frequency of 28KHz, and then dry it at 80°C for 11 hours;

[0038] B. The catalyst after drying in step A is impregnated with impregnating solution for 20 minutes under the same ultrasonic assisted conditions as above, and then dried at 60° C. for 12 hours. The impregnating solution is 7 g of NaOH dissolved in 50 ml of water. solution;

[0039] C. Place the catalyst obtained in step B in a muffle furnace, bake it for 1.2h at a temperature of 400°C, and control the heating rate to 5°C / min to obtain a regenerated catalyst, whose activity is shown in figure 2 .

Embodiment 3

[0041] A. Wash 2 g of the deactivated catalyst with distilled water for 40 minutes on a conventional ultrasonic instrument at a temperature of 30°C and a frequency of 40KHz, and then dry it at 70°C for 10 hours;

[0042] B. The catalyst dried in step A is impregnated with impregnating solution for 30 minutes under the same ultrasonic-assisted conditions as above, and then dried at 80°C for 10 hours. The impregnating solution is 5.2995 g of Na 2 CO 3 A solution obtained by dissolving in 50ml of water;

[0043]C. Place the catalyst obtained in step B in a muffle furnace, and bake it for 2 hours at a temperature of 350°C, with a heating rate of 5°C / min, to obtain a regenerated catalyst, whose activity is shown in image 3 .

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Abstract

The invention provides a method for regenerating a carbonyl sulfide hydrolysis catalyst after inactivation. The method comprises the following steps of: washing an inactivated catalyst by using water under the ultrasonic assistant condition for 20 to 40 min, and drying at the temperature of between 60 and 80 DEG C for 10 to 12 h; impregnating by using impregnation liquid under the ultrasonic assistant condition for 20 to 40 min, and drying at the temperature of between 60 and 80 DEG C for 10 to 12 h; putting the inactivated catalyst into a muffle furnace, roasting under the condition that thetemperature is between 250 and 450 DEG C and the heating rate is 5 DEG C / min for 1 to 3 h to obtain a regenerated catalyst. The regeneration method adopted by the invention has the advantages of simple process, particularly relatively low roasting temperature, energy saving and easy industrial production; an alkali metal compound in the used impregnation liquid is cheap in price and readily available, and has low cost, high catalytic activity after regeneration and multiple regeneration; and the catalyst regenerated by the invention can ensure that the carbonyl sulfide (COS) conversion rate reaches over 90 percent.

Description

technical field [0001] The invention relates to a regeneration method of a deactivated catalyst, in particular to a regeneration method of a deactivated low-temperature carbonyl sulfide hydrolysis catalyst. Background technique [0002] COS is the main form of organic sulfur in industrial gases. Trace amounts of COS in industrial production can easily cause catalyst poisoning and deactivation, and have a corrosive effect on industrial production equipment. In addition, COS emitted to the atmosphere without treatment can form SO 2 , promote photochemical reactions, and eventually transform into sulfate aerosols, causing serious environmental problems. Recently, the research on the removal of COS is mostly hydrolysis method. Under the action of hydrolysis catalyst, the water vapor in the tail gas or raw material gas is used to convert COS into easier-to-handle inorganic hydrogen sulfide (H 2 S), and then hydrogen sulfide is removed by other means. [0003] CN1069673A disclo...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/94B01D53/90B01D53/48
Inventor 易红宏王红妍唐晓龙宁平于丽丽何丹赵顺征
Owner KUNMING UNIV OF SCI & TECH