Abstract:
The invention concerns a process for desulphurization of a gaseous effluent containing hydrogen sulphide using a Claus treatment unit followed by a Claus tail gas treatment unit (TGT), said process comprising using a device for on-line analysis of the ratio H2S/SO2 at the outlet from the TGT unit and a feed-back loop which can maintain said H2S/SO2 molar ratio at the outlet from the TGT unit to a value close to 2 and generally in the range 1.5 to 2.5.
Abstract translation:本发明涉及使用克劳斯处理单元和克劳斯尾气处理单元(TGT)对含有硫化氢的气态流出物进行脱硫的方法,所述方法包括使用在线分析H2S / SO2比例的装置 来自TGT单元的出口和能够将来自TGT单元的出口处的所述H 2 S / SO 2摩尔比保持在接近2并且通常在1.5至2.5的范围内的反馈回路。
Abstract:
A process for treating a gas containing hydrogen sulphide (H2S) and sulphur dioxide (SO2) is described in which: said gas is brought into contact at a suitable temperature with an organic solvent containing at least a soluble catalytic system, comprising at least one compound comprising at least one functional group A consisting of a carboxylic acid function and at least one functional group B comprising at least one nitrogen atom and which can produce an acid-base type reaction with at least one functional group A under the operating conditions of said process; a gaseous effluent substantially depleted in hydrogen sulphide and sulphur dioxide is recovered, along with liquid sulphur separated from the solvent by liquid-liquid decantation; said catalytic system which is employed slowing by-product formation.
Abstract translation:描述了一种处理含硫化氢(H 2 S 2 S)和二氧化硫(SO 2 H 2)的气体的方法,其中:所述气体在合适的温度下接触 含有至少一种可溶性催化体系的有机溶剂,其包含至少一种包含至少一种由羧酸官能团组成的官能团A和至少一种包含至少一个氮原子的官能团B的化合物,该官能团可以产生酸 - 在所述方法的操作条件下与至少一个官能团A的碱型反应; 回收基本上不含硫化氢和二氧化硫的气态流出液以及通过液 - 液倾析与溶剂分离的液态硫; 所述催化系统用于减缓副产物形成。
Abstract:
The invention concerns a process for desulphurization of a gaseous effluent containing hydrogen sulphide using a Claus treatment unit followed by a Claus tail gas treatment unit (TGT), said process comprising using a device for on-line analysis of the ratio H2S/SO2 at the outlet from the TGT unit and a feed-back loop which can maintain said H2S/SO2 molar ratio at the outlet from the TGT unit to a value close to 2 and generally in the range 1.5 to 2.5.
Abstract translation:本发明涉及使用克劳斯处理单元和克劳斯尾气处理单元(TGT)对含有硫化氢的气态流出物进行脱硫的方法,所述方法包括使用在线分析H2S / SO2比例的装置 来自TGT单元的出口和能够将来自TGT单元的出口处的所述H 2 S / SO 2摩尔比保持在接近2并且通常在1.5至2.5的范围内的反馈回路。
Abstract:
The mercaptan-laden natural gas is contacted with a mercaptan-adsorbing sieve T1. The mercaptan-rich gaseous effluent obtained upon regeneration of sieve T2 is then contacted with an olefin-containing liquid feed in the presence of an acid catalyst. Under suitable conditions, the mercaptans are absorbed in the liquid feed and they react with the olefins so as to form solvent-soluble sulfides. A solvent regeneration stage allows the capture agent to be recycled.
Abstract:
A process for treating a gas containing hydrogen sulphide (H2S) and sulphur dioxide, contacting the gas at a suitable temperature with an organic solvent containing at least a soluble catalytic system, comprising at least one compound comprising at least one functional group A consisting of a carboxylic acid function and at least one functional group B comprising at least one nitrogen atom and which can produce an acid-base type reaction with at least one functional group A under the operating conditions of said process; and recovering a gaseous effluent substantially depleted in hydrogen sulphide and sulphur dioxide along with liquid sulphur separated from the solvent by liquid-liquid decantation.
Abstract:
The gaseous feed flowing in through line 1 is contacted in contacting zone ZA with a liquid solvent flowing in through line 2. The solvent comprises between 0.001% and 100% by weight of a liquid olefin. Contacting in zone ZA is carried out in the presence of an acid catalyst. The purified gaseous feed is discharged from zone ZA through line 3. The sulfide-laden solvent is discharged through line 4, then regenerated in unit RE. The regenerated solvent is recycled through lines 7 and 2 to zone ZA.
Abstract:
The mercaptan-laden natural gas is contacted with a mercaptan-adsorbing sieve T1. The mercaptan-rich gaseous effluent obtained upon regeneration of sieve T2 is then contacted with an olefin-containing liquid feed in the presence of an acid catalyst. Under suitable conditions, the mercaptans are absorbed in the liquid feed and they react with the olefins so as to form solvent-soluble sulfides. A solvent regeneration stage allows the capture agent to be recycled.
Abstract:
The gaseous feed flowing in through line 1 is contacted in contacting zone ZA with a liquid solvent flowing in through line 2. The solvent comprises between 0.001% and 100% by weight of a liquid olefin. Contacting in zone ZA is carried out in the presence of an acid catalyst. The purified gaseous feed is discharged from zone ZA through line 3. The sulfide-laden solvent is discharged through line 4, then regenerated in unit RE. The regenerated solvent is recycled through lines 7 and 2 to zone ZA.