← Back to Patent Explorer
US3634037A Expired / Lapsed US ⏱️ 0.0 years remaining

Treatment of a water stream containing ammonium sulfide salts

Assignee: Universal Oil Products Co
•
Filing: 1968-12-23
•
Granted: 1972-01-11
•
Expires: 1988-12-23
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A water stream containing NH4HS is treated to produce elemental sulfur, an ammoniacal aqueous stream and a treated water stream by the steps of: (a) catalytically treating the water stream with an airstream to produce an effluent stream containing ammonium polysulfide, N2 and unreacted NH4HS; (b) separating the effluent stream from step (a) into a vent gas stream and a water stream; (c) decomposing the polysulfide contained in the water stream from step (b) to produce a vapor stream and a bottom stream containing elemental sulfur; (d) separating sulfur from the bottom stream from step (c) to form a treated water stream; (e) recovering a first portion of the treated water stream from step (d) as a product stream; (f) using a second portion of the treated water stream from step (d) to scrub the vent gas stream from step (b) in order to remove NH3 and H2S therefrom; (g) fractionating the overhead vapor stream from step (c) and the bottom stream from the scrubbing step to form an ammoniacal aqueous overhead stream and an aqueous bottom stream containing essentially all of the unreacted sulfide present in the effluent stream from the treating step; and, (h) recycling the bottom stream from step (g) to step (a). Key feature is the use of a scrubbing step on the vent gases from the treating step operated at a relatively low pressure and a relatively high-liquid gas loading, coupled with a combination scrubbing and fractionating step on the bottom stream from the scrubbing step and on the vapor stream from the polysulfide decomposition step. This combination scrubbing and fractionating step is operated at a relatively high pressure, thereby increasing the amount of H2S that can be absorbed. The principle advantages of the resulting process are significant improvements in the amount of ammonia and sulfur recovered and a substantial simplification of the overall process.

Inventors

  • 👤 Robert J J Hamblin

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 10:12
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/72; C02F1/725; C01; C01B; C01B17/00; C01B17/02; C01B17/06; C01C; C01C1/00; C01C1/20

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 18 words
A process as defined in claim 1 wherein the catalyst utilized in step (a) is a phthalocyanine catalyst.
Claim 2
Dependent Claim 25 words
A process as defined in claim 1 wherein the catalyst utilized in step (a) comprises an iron group metallic sulfide combined with a carrier material.
Claim 3
Dependent Claim 25 words
A process as defined in claim 1 wherein the catalyst utilized in step (a) is cobalt phthalocyanine monosulfonate combined with an activated carbon carrier material.
Claim 4
Dependent Claim 33 words
A process as defined in claim 1 wherein the amount of oxygen charged to step (a) is sufficient to react about 0.4 mols of oxygen per mol of sulfide charged to said step.
Claim 5
Dependent Claim 50 words
A process as defined in claim 1 wherein the oxidizing conditions utilized in step (a) include a temperature of about 80* to about 300* F., a pressure of about 1 to about 10 p.s.i.g. and a combined stream liquid hourly space velocity of about 1.0 to about 10.0 hr. 1.
Claim 6
Dependent Claim 32 words
A process as defined in claim 1 wherein the polysulfide decomposition conditions include a temperature of about 200* to about 350* F. and a pressure of about 15 to about 75 p.s.i.g.
Claim 7
Dependent Claim 41 words
A process as defined in claim 1 wherein the concentration of ammonium hydrosulfide in the aqueous waste stream plus the aqueous recycle stream being charged to step (a) is about 4 to about 8 weight percent on a combined stream basis.
Claim 8
Dependent Claim 39 words
A process as defined in claim 1 wherein said relatively low pressure used in step (f) is about 1 to 10 p.s.i.g. and wherein said relatively high pressure utilized in step (g) is about 15 to about 75 p.s.i.g.

References Cited (Backward Citations)

US1656563A Cited
US3335071A Cited
US3457046A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-01-10 1975-07-12 1976-01-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-01-10 1979-07-12 1980-01-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-01-10 1983-07-12 1984-01-11 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag