Low-temperature micro-oxygen purification method for removing harmful gas in yellow phosphorus tail gas

A technology for harmful gases and yellow phosphorus tail gas, applied in chemical instruments and methods, separation methods, separation of dispersed particles, etc., can solve problems such as poor adaptability, effective utilization rate of less than 30%, poisoning of oxo catalysts, etc.

Inactive Publication Date: 2009-01-28
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

These impurities can lead to poisoning of carbonylation catalysts, and the yellow phosphorus tail gas must be removed when used as a carbon chemical raw material gas. At present, most of the yellow phosphorus tail gas is burned and discharged, and the effective utilization rate is less than 30%.
The process of this method is more complicated and the adaptability is poor
[0007]

Method used

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  • Low-temperature micro-oxygen purification method for removing harmful gas in yellow phosphorus tail gas
  • Low-temperature micro-oxygen purification method for removing harmful gas in yellow phosphorus tail gas
  • Low-temperature micro-oxygen purification method for removing harmful gas in yellow phosphorus tail gas

Examples

Experimental program
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Effect test

Embodiment 1

[0062] Make the flow rate 300ml / min containing HCN100mg / m 3 、COS 800mg / m 3 、PH 3 750mg / m 3 、H 2 S 800mg / m 3 、CS 2 40mg / m 3 The mixed gas enters heat exchanger 1 to heat the furnace gas to 150°C; enters HCN and COS, CS 2 Hydrolyzer 2, converts HCN to NH 3 , COS and CS 2 converted to H 2 S, the catalyst uses DJ-1 multi-functional purifier and EZX multi-functional conversion and absorption fine desulfurizer, both of which have a mass of 2.00g and are respectively filled in two layers of the packed tower with a space velocity of 4000h -1 ; Then the furnace gas enters the selective catalytic oxidation reactor 4 after being cooled to 80°C through the cooling tower 3, and the pH 3 and H 2 Catalytic oxidation of S to P 2 o 5 and S, using a dual-functional high-selectivity catalyst developed by Kunming University of Science and Technology, the catalyst component is 20g ZP-3 type activated carbon, and the supported 100ml concentration is 0.05mol / L Cu(Ac) 2 After soaking in...

Embodiment 2

[0064] Make the flow rate 400ml / min containing HCN 350mg / m 3 、COS 1000mg / m 3 、PH 3 1000mg / m 3 、H 2 S1000mg / m 3 、CS 2 80mg / m 3 The mixed gas enters the heat exchanger 1 through the intake pipe, heats the furnace gas to 200°C, and enters HCN and COS, CS 2 Hydrolyzer 2, converts HCN to NH 3 , COS and CS 2 converted to H 2 S, the catalyst adopts DJ-1 multifunctional purifying agent and the catalyst in Chinese patent CN1095963A, both of which have a mass of 2.00g and are respectively filled in two layers of the packed tower with a space velocity of 5000h -1 ; Then the furnace gas enters the selective catalytic oxidation reactor 4 after being cooled to 80°C through the cooling tower 3, and the pH 3 and H 2 Catalytic oxidation of S to P 2 o 5 and S, using a dual-functional high-selectivity catalyst developed by Kunming University of Science and Technology, the catalyst component is 20g JH-3 type activated carbon, loaded with 100ml of Cu(Ac)2 solution with a concentrati...

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Abstract

The invention provides a micro-oxygen purifying method used for removing harmful gas in yellow phosphorus tail gas, which is characterized in that mixed gas containing HCN, PH, H2S, COS and CS2, with the speed of 1000-5000/h is heated to 150-200 DEG C by a heat exchanger and sent to a catalytic hydrolysis reactor; more than 90% of HCN and 85% of COS and CS2 can be respectively hydrolysed as NH3, CO, H2S and CO2; subsequently, the mixed gas enters a selective catalytic oxidation reaction; PH3 and H2S are catalysed and oxidated as P2O5 and S; harmful gas in the mixed gas which is disposed twice is removed further in a fine decyanation reactor and the sulfide thereof is removed by a fine desulfurization reactor; NH3 is selectively catalysed and oxidated as N2, thus purifying the mixed gas. The method of the invention leads the violent toxic matter to be converted into non-toxic matter, generates no secondary pollution, recovers the outgrowth sulphur, improves the utilization ratio of the resource, eliminates the environmental pollution due to waste gas exhausting, and has the advantages of simple process, few investment and low running expense.

Description

technical field [0001] The invention relates to a method for simultaneously removing toxic and harmful gases hydrogen cyanide (HCN) and phosphine (PH) from yellow phosphorus tail gas. 3 ), carbonyl sulfide (COS), hydrogen sulfide (H 2 S), carbon disulfide (CS 2 )Methods. Background technique [0002] The main component of yellow phosphorus tail gas is CO, impurity H 2 1% ~ 8%, O 2 0.5%~1%,H 2 O 1%~5%, CH 4 0.3%, N 2 1%~5%, HCN 100~350mg / Nm 3 ,PH 3 750~1200mg / Nm 3 , H 2 S 800~1100mg / Nm 3 , COS 700~1000mg / Nm 3 , CS 2 20~80mg / Nm 3 . HCN and PH in yellow phosphorus tail gas 3 It is not only a highly toxic gas that is harmful to the environment and endangers human health, but also restricts production process control, safe production and comprehensive utilization of waste. These impurities can lead to poisoning of the oxo catalyst. The yellow phosphorus tail gas must be removed when used as a carbon chemical raw material gas. At present, most of the yellow ...

Claims

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Application Information

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IPC IPC(8): B01D53/86B01D53/75B01D53/46
Inventor 唐晓龙宁平易红宏于丽丽王先厚孔渝华田森林张清建
Owner KUNMING UNIV OF SCI & TECH
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