Process for preparing sulfuric acid by sulfurated hydrogen stepwise reaction

A hydrogen sulfide and sulfuric acid production technology, which is applied in the field of coal chemical industry, can solve the problems of complex process, difficult to use hydrogen sulfide to prepare sulfuric acid process, difficult operation and increased investment

Inactive Publication Date: 2009-07-15
SHANDONG UNIV OF SCI & TECH
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Problems solved by technology

The Kangkaite method is suitable for producing sulfuric acid from low-concentration hydrogen sulfide. Two-stage Venturi condensers, condensation towers, wire mesh and fiber demisters are used to recover sulfuric acid to obtain 93% concentrated sulfuric acid. The process is complex, the process is long, and the concentration of sulfuric acid is low.
The WSA-2 wet decomposition contact method is suitable for treating 40%-50% hydrogen sulfide gas at a high concentration. The combustion of hydrogen sulfide and the oxidation of sulfur dioxide are carried out in the same reactor...

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  • Process for preparing sulfuric acid by sulfurated hydrogen stepwise reaction

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Embodiment Construction

[0010] The present invention is described in detail below in conjunction with accompanying drawing: raw material hydrogen sulfide gas and the air that is about 40% hydrogen sulfide gas combustion to generate sulfur dioxide pass burner 1 and incomplete combustion takes place at the front of air-cooled reactor 2, and the mixed gas that produces Further reaction and combustion with the cooling air entering along the inner wall 3 of the air-cooled reactor, the hydrogen sulfide is completely converted into sulfur dioxide; the sulfur dioxide product gas passes through the waste heat boiler 13 to generate high-pressure steam to recover heat, and then enters the converter 4; the sulfur dioxide product gas passes through the converter 4 The 3-stage or 4-stage catalyst bed layer 6 catalytically oxidizes to generate sulfur trioxide, and the heat released by each layer of reaction is diluted and cooled by air from 2 or 3 quenching air inlets 5 between the layers to keep the reaction tempera...

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Abstract

The invention provides a process for preparing sulphuric acid by the step reaction of sulfureted hydrogen. Raw material of sulfureted hydrogen and part of air are burnt incompletely at the front part of an air cooled reactor through a burner, generated mixing gas and cooled air entering along the internal wall of the reactor are burnt further, the sulfureted hydrogen is completely converted into sulfur dioxide; the sulfur dioxide passes through a waste heat boiler to generate high pressure steam for recycling the heat quantity and enters a convertor; the sulfur dioxide is catalyzed and oxidized into sulfur trioxide in a converter by adopting the way of subsection air sharp quenching; and the sulfur trioxide gas is absorbed into a concentration tower, higher than 97 percent sulphuric acid is obtained at the bottom of the tower and the tail gas at the top of the tower is purified and discharged.

Description

1. Technical field [0001] The invention provides a process for producing sulfuric acid by stepwise reaction of hydrogen sulfide, which belongs to the field of coal chemical industry. 2. Background technology [0002] At present, the hydrogen sulfide produced by the coal chemical industry is mainly produced by the Claus method, that is, the hydrogen sulfide is firstly oxidized to sulfur dioxide by air, and the H 2 S / SO 2 Under the condition of the molar ratio of 2:1, it reacts with the catalyst to generate sulfur; in order to prevent environmental pollution, it is necessary to build a huge tail gas treatment device, so the construction investment and production cost of the sulfur production device are very high. However, more than 90% of the sulfur produced at such a high cost is used as a raw material for the production of sulfuric acid. If hydrogen sulfide is used to directly produce sulfuric acid, many complicated processes can be saved, and the production cost of sulfur...

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Application Information

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IPC IPC(8): C01B17/69C01B17/76
CPCY02P20/129
Inventor 田原宇乔英云盖希坤梁鹏黄伟
Owner SHANDONG UNIV OF SCI & TECH
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