Process for the conversion of polysulfanes
The invention provides a process for the removal of polysulfanes from gas streams formed during H 2 S synthesis.
1. A process for obtaining a purified gas by removing polysulfanes from crude gas formed during the production of hydrogen sulfide, wherein said crude gas comprises greater than 80% by volume of H 2 S and 100-2000 vpm of polysulfanes of the formula H 2 S n , wherein n=2-8, said process comprising:
a) passing said crude gas through a wash system where said crude gas is brought into contact with a wash solution comprising water or methanol; and
b) collecting said purified gas from the wash solution of step a).
2. The process of claim 1 , wherein said polysulfanes are present in said crude gas at 400–1500 vpm.
3. The process of claim 1 , wherein said wash system is a jet washer.
4. The process of claim 1 , further comprising a second wash step in which the purified gas produced in step a) is passed through a counter-current washer comprising an aqueous or methanolic solution.
5. The process of claim 1 , further comprising a second wash step in which the purified gas produced in step a) is passed through an adsorber bed.
6. The process of claim 1 , wherein relative to said crude gas, the polysulfanes in said purified gas have been reduced by 50–99.5%.
7. The process of claim 1 , wherein said process is carried out at a temperature of 0–150° C.
8. A process for obtaining a purified gas by removing polysulfanes from crude gas formed during the production of hydrogen sulfide, wherein said crude gas comprises greater than 80% by volume of H 2 S and 100-2000 vpm of polysulfanes of the formula H s S n , wherein n=2-8, and wherein said process comprises:
a) passing said crude gas through a wash system comprising an aqueous or methanolic solution containing 0.5–20 wt % of an alkali or alkaline earth hydroxide or oxide; and
b) collecting said purified gas from the aqueous or methanolic solution of step a).
9. The process of claim 8 , wherein said polysulfanes are present in said crude gas at 400–1500 vpm.
10. The process of claim 8 , wherein relative to said crude gas, the polysulfanes in said purified gas have been reduced by 50–99.5%.
11. The process of claim 8 , wherein said wash system is a jet washer and said process further comprises a second wash step in which the purified gas of step a) is passed through either: a counter-current washer comprising an aqueous or methanolic solution; or an adsorber bed.
12. A process for obtaining a purified gas by removing polysulfanes from crude gas formed during the production of hydrogen sulfide, wherein said crude gas comprises greater than 80% by volume of H 2 S and 100-2000 vpm of polysulfanes of the formula H 2 S n , wherein n=2-8, and wherein said process comprises
a) passing said crude gas through a wash system comprising an aqueous or methanolic solution containing 1–20 wt % of a compound selected from the group consisting of:
i) an organic amine of the formula (C n H 2n+1 ) x NH y , where n=1–3, x=2 or 3, and y=0 or 1;
ii) an amino alcohol of formula (C n H 2n+1 O) x NH y , where n=1–3, x=2 or 3, and y=0 or 1; and
iii) ammonia;
b) collecting said purified gas from the aqueous or methanolic solution of step a).
13. The process of claim 12 , wherein said compound is an organic amine of the formula (C n H 2n+1 ) x NH y , where n=1–3, x=2 or 3, and y=0 or 1.
14. The process of claim 12 , wherein said compound is an amino alcohol of formula (C n H 2 2n+1 O) x NH y , where n=1–3, x=2 or 3, and y=0 or 1.
15. The process of claim 12 , wherein said compound is ammonia.
16. The process of claim 12 , wherein relative to said crude gas, the polysulfanes in said purified gas have been reduced by 50–99.5%.
17. The process of claim 12 , wherein said wash system is a jet washer and said process further comprises a second wash step in which the purified gas of step a) is passed through either: a counter-current washer comprising an aqueous or methanolic solution; or an adsorber bed.