Solubility of Hydrogen Sulfide in Aqueous Solutions of N-Methyldiethanolamine and Piperazine

2012 ◽  
Vol 51 (38) ◽  
pp. 12549-12556 ◽  
Author(s):  
Dirk Speyer ◽  
Arne Böttger ◽  
Gerd Maurer
1980 ◽  
Vol 127 (6) ◽  
pp. 1228-1235 ◽  
Author(s):  
D. R. Morris ◽  
L. P. Sampaleanu ◽  
D. N. Veysey

1996 ◽  
Vol 41 (5) ◽  
pp. 1181-1183 ◽  
Author(s):  
Fang-Yuan Jou ◽  
Frederick D. Otto ◽  
Alan E. Mather

2014 ◽  
Vol 89 (1) ◽  
pp. 19-23 ◽  
Author(s):  
A. N. Startsev ◽  
O. V. Kruglyakova ◽  
Yu. A. Chesalov ◽  
A. N. Serkova ◽  
E. A. Suprun ◽  
...  

2015 ◽  
Vol 393 ◽  
pp. 33-39 ◽  
Author(s):  
Negar Sadegh ◽  
Kaj Thomsen ◽  
Even Solbraa ◽  
Eivind Johannessen ◽  
Gunn Iren Rudolfsen ◽  
...  

2019 ◽  
Vol 13 (1) ◽  
pp. 46-67
Author(s):  
Warren Reátegui-Romero ◽  
Fredy Castillejo-Melgarejo ◽  
María E. King-Santos

Background: This research deals with the manufacture of sodium sulphides and sodium sulfhydrate in an isothermal multiphase chemical reactor to produce concentrated aqueous solutions of sodium sulfhydrate (greater than 43%) through Gas-Liquid-Solid reactions from hydrogen sulfide and hydroxide of sodium at 50%. Methods: A method is proposed that integrates the recovery of hydrogen sulfide from an industrial chemical process where the H2S gas is generated as a sub product, the strategy of the developed process was integrated into a manufacturing plant of dithiophosphoric acids (ADTF) where it was possible to recover the hydrogen sulfide in the form of an aqueous solution of NaHS with a concentration higher than 43%. Results: The experimental tests showed that the biphasic reaction mixture formed by Na2S, NaHS and H2O with global compositions of 13.3%; 26.9% and 59.7% respectively, is appropriate to obtain 43% sodium sulfhydrate in a stirred tank reactor, operated at temperatures ranging from 50°C to 55°C, where gaseous hydrogen sulfide is continually bubbled. Conclusion: Sodium sulfide (specifically Na2S.5H2O crystals) of the biphasic mixture is produced from a solution of sodium sulfhydrate (43% NaHS) and aqueous sodium hydroxide (50% NaOH). The environmental problem generated by the H2S was solved with a 90% recovery in the multiphase reactor and 5% in the safety absorber.


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