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Claus tail gas condensing treatment process

A Claus tail gas and treatment process technology, applied in the field of Claus tail gas condensation treatment process, can solve problems such as increased energy consumption, and achieve the effects of increasing gas volume, reducing steam consumption and saving energy

Pending Publication Date: 2017-12-26
ACRE COKING & REFRACTORY ENG CONSULTING CORP DALIAN MCC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Practice shows that, taking the scale of annual production of 3 million tons of coke as an example, the N 2 The content increases by 2-3%, and the energy consumption increases by about 200KW in the process of producing methanol and LNG

Method used

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  • Claus tail gas condensing treatment process

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Embodiment Construction

[0031] The specific embodiment of the present invention will be further described below in conjunction with accompanying drawing:

[0032] like figure 1 Shown, a kind of Claus tail gas condensation treatment process of the present invention comprises the steps:

[0033] 1) The temperature of the Claus tail gas coming out of the Claus process sulfur condenser is 130-160°C, controlled by the program-controlled valve 3, firstly enters the shell side of the heat exchanger-1, and passes into the tube side of the heat exchanger-1 for cooling Water cooling, the gaseous sulfur in the Claus tail gas is condensed on the outer surface of the heat exchange tube to be removed;

[0034] 2) The Claus tail gas from which gaseous sulfur has been removed is sent to the desulfurization absorption tower 5, and the desulfurization absorption tower 5 is sprayed with the desulfurization liquid from the gas purification device; most of the H in the Claus tail gas 2 S, SO 2 , CO 2 Absorbed by the ...

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Abstract

The invention relates to a Claus tail gas condensing treatment process, which comprises the steps that Claus tail gas coming from a Claus process sulfur condenser enters a heat exchanger I, gaseous sulfur is condensed and removed; the gaseous sulfur-removed Claus tail gas is sent to a desulfurizing absorption tower and is sprayed by adopting a doctor solution coming from a gas purification device, rich liquor is returned to the gas purification device for regeneration, and regenerated acid gas is used as a raw material for a Claus process; the upper part of the desulfurizing absorption tower is provided with an alkali washing section, and alkali liquor is a replenishing solution coming from a desulfurizing unit of the gas purification device; after the removal of H2S, the Claus tail gas is sent to a coke oven gas system or is returned to a returned gas system; the heat exchanger I and a heat exchanger II work in a cyclic alternating pattern, and the continuous condensing of the gaseous sulfur in the Claus tail gas is realized. The Claus tail gas condensing treatment process has the remarkable advantages of small investment, low operating cost, energy conservation, greenness, environmental protection and the like.

Description

technical field [0001] The invention relates to the technical field of recovery of coking chemical products, in particular to a Claus tail gas condensation treatment process. Background technique [0002] At present, the Claus process in the coking industry has no tail gas treatment measures, and its tail gas is blended back to the coke oven gas system. [0003] The Claus process in the coking industry usually consists of a combustion section and a one-stage and two-stage catalytic section. By controlling the H in the combustion section 2 The incomplete combustion ratio of S makes 1 / 3 of H 2 S generates SO 2 , H 2 S and SO 2 This produces elemental sulfur. To the catalytic section, under the action of the catalyst, H 2 S and SO 2 Stoichiometric reaction generates elemental sulfur; then condenses the generated gaseous sulfur into liquid sulfur for separation. [0004] In the Claus reaction, its progress is limited by the reaction temperature, chemical equilibrium, rev...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/50B01D53/52B01D53/00B01D53/62C01B17/04
CPCB01D53/002B01D53/502B01D53/523B01D53/62B01D53/78C01B17/0456B01D2257/504B01D2257/304B01D2257/302Y02P20/10Y02P20/151
Inventor 张素利刘开源魏冰徐作锋
Owner ACRE COKING & REFRACTORY ENG CONSULTING CORP DALIAN MCC
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