US4056469A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Purification of waste water from hydrazine production
Assignee: Bayer AG
•
Filing: 1976-06-15
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Granted: 1977-11-01
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Expires: 1996-06-15
Abstract
Abstract A process for the purification of waste water produced in hydrazine production by the oxidation of ammonia or an amine with an oxidizing agent in the presence of an aldehyde or ketone, comprising intensively mixing the waste water with chlorine or a hypochlorite at a temperature of about 10° C to 110° C and a pH of about 5 to 10 until the treated waste water reaches a redox potential to platinum, relative to Ag/AgCl, of about -400 mV to +800 mV. Advantageously a small amount of waste water is distilled off both before and after the chlorine or hypochlorite treatment.
Inventors
- 👤 Kurt-Wilhelm Eichenhofer
- 👤 Reinhard Schliebs
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 16:30
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/72; C02F1/76
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
93 words
A process for the purification of waste water produced in hydrazine production by the oxidation of ammonia or amine with an oxidizing agent in the presence of an aldehyde or ketone, such waste water containing small amounts of hydrazine and organic hydrazine derivatives, comprising intensively mixing the waste water with chlorine or a hypochlorite at a temperature of about 10° C to 110° C and a pH of about 5 to 10 until the treated waste water reaches a redox potential to platinum, relative to Ag/AgCl, of about -400 mV to +800 mV.
Claim 2
Dependent Claim
93 words
A process for the purification of waste water produced in hydrazine production by the oxidation of ammonia or amine with an oxidizing agent in the presence of an aldehyde or ketone, such waste water containing small amounts of hydrazine and organic hydrazine derivatives, comprising intensively mixing the waste water with chlorine or a hypochlorite at a temperature of about 10° C to 110° C and a pH of about 5 to 10 until the treated waste water reaches a redox potential to platinum, relative to Ag/AgCl, of about -400 mV to +800 mV.
Claim 3
Dependent Claim
19 words
A process according to the claim 1, wherein chlorination or hypochlorination is conducted for about 1 to 30 minutes.
Claim 4
Dependent Claim
26 words
A process according to claim 1, wherein the waste water initially contains hydrazine and organic hydrazine derivatives (calculated as hydrazine) in about 100 to 1000 ppm.
Claim 5
Dependent Claim
53 words
A process according to claim 1, wherein the waste water is treated at a temperature of about 60° to 100° C and a pH of about 6 to 9 with chlorine or hypochlorite until the treated waste water reaches a redox potential to platinum, relative to Ag/AgCl, of about -200 to +700 mV.
Claim 6
Dependent Claim
32 words
A process according to claim 1, wherein chlorination or hypochlorination is carried out until an ammonia or ammonium content of less than about 0.1% by weight is reached in the waste water.
Claim 7
Dependent Claim
26 words
A process according to claim 1, wherein before treatment with chlorine or hypochlorite up to about 10% by volume of the waste water is distilled off.
Claim 8
Dependent Claim
26 words
A process according to claim 1, wherein after treatment with chlorine or hypochlorite up to about 1% by volume of the treated water is distilled off.
Claim 9
Dependent Claim
31 words
A process according to claim 1, wherein the treated waste water containing sodium chloride is subjected to a chlorine-alkali-electrolysis and the chlorine and caustic soda formed are recycled to hydrazine production.
Claim 10
Dependent Claim
112 words
A process according to claim 1, wherein the waste water initially contains hydrazine and organic hydrazine derivatives (calculated as hydrazine) in about 100 to 1000 ppm, before treatment with chlorine or hypochlorite up to about 10%, by volume of the waste water is distilled off, the waste water is treated at a temperature of about 70° to 90° C and a pH of about 7 to 8.5 with chlorine or hypochlorite for about 1 to 10 minutes until the treated waste water reaches a redox potential to platinum, relative to Ag/AgCl, of about +100 to +600 mV, and up to about 1% by volume of the treated water is then distilled off.
References Cited (Backward Citations)
US3767572A
Cited
US3923648A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-10-31 | 1981-05-02 | 1981-11-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-10-31 | 1985-05-02 | 1985-11-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-10-31 | 1989-05-02 | 1989-11-01 | $7700.00 | Window Closed / Lapsed |