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What is the acceptable level of H2S content in the rich and lean liquids?

2009-09-24View Original

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This post was last edited by Tianya Langji on 2009-12-25 at 20:26. What is the acceptable level of H2S content in Fugubaiye?
Reply #22009-09-24
This post was last edited by adsl121 on 2009-9-25 01:20. What is sh2?
Reply #32009-09-24
The H2S levels in the rich and lean fluids vary depending on the different units used. For hydrogenation units, a H2S level in the lean liquid of ≮2 g/l is generally sufficient, while the H2S level in the rich liquid is usually around 20–30 g/l. As for the lean liquid required for the exhaust gases from sulfur recovery units, a level of ≮1 g/l is typical, with the H2S level in the rich liquid being around 4–10 g/l.
Reply #42009-09-25
In our unit, the hydrogen sulfide content in the lean liquid is not more than 0.1 mg/l, and the carbon dioxide content is not more than 1 mg/l
Reply #52009-09-25
Are the indicators mentioned upstairs true? That’s world-class level!
Reply #62009-10-22
4# adsl121 What are your metrics? What is it used for?
Reply #72009-12-14
The hydrogen sulfide content in the lean liquid should not exceed 0.1 mg/l; the performance of various technologies in this regard is quite high. Our standard for precise desulfurization is 0.03 PPM
Reply #82009-12-24
The lean liquid required for the exhaust gas from our sulfur recovery unit is usually ≮1g/l, while the H2S concentration in the rich liquid is generally between 4-10g/l.
Reply #92009-12-25
Generally, the requirement for lean liquid in sulfur plants is no more than 1 G/L
Reply #102009-12-25
Generally, the indicators for sulfur recovery are this low; otherwise, it will cause foaming in the amine solution.

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