US5401485A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Reduction of residual chloride in iron oxides
Assignee: BASF Corp
•
Filing: 1994-03-15
•
Granted: 1995-03-28
•
Expires: 2014-03-15
Abstract
Abstract A process for reducing the residual chloride present in iron oxides, particularly in regenerated iron oxides produced from hydrochloric acid waste liquid generated from steel pickling, by post-synthesis treatment of the iron oxides with sulfuric acid optionally followed by drying and calcining. The purified regenerated iron oxides are particular suitable for making iron oxide based catalysts such as ethylbenzene dehydrogenation catalysts and high-grade ferrites.
Inventors
- 👤 David M. Hamilton, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 19:55
CPC Classifications
B; B01; B01J; B01J37/00; B01J37/06; B01J23/00; B01J23/70; B01J23/74; B01J23/745; C; C01; C01G; C01G49/00; C01G49/02; C01P; C01P2006/00; C01P2006/80; Y; Y10; Y10S; Y10S423/00; Y10S423/01
Claims Analysis
Total Claims: 22
Claim 1
Independent Claim
69 words
A process for removing chloride from a chloride-containing iron oxide, which process comprises the steps of: (a) mixing the chloride-containing iron oxide with an aqueous solution comprising a molar amount of H 2 SO 4 from about 0.5 to about 5 times the molar amount of chloride in the chloride-containing iron oxide to form a mixture; and (b) separating the iron oxide from said mixture formed in step (a).
Claim 2
Dependent Claim
69 words
A process for removing chloride from a chloride-containing iron oxide, which process comprises the steps of: (a) mixing the chloride-containing iron oxide with an aqueous solution comprising a molar amount of H 2 SO 4 from about 0.5 to about 5 times the molar amount of chloride in the chloride-containing iron oxide to form a mixture; and (b) separating the iron oxide from said mixture formed in step (a).
Claim 3
Dependent Claim
46 words
The process as described in claim 1, wherein the solution comprising H 2 SO 4 used in step (a) comprises a molar amount of H 2 SO 4 of from about 0.5 to about 2.5 times the molar amount of chloride in the chloride-containing iron oxide.
Claim 4
Dependent Claim
46 words
The process as described in claim 1, wherein the solution comprising H 2 SO 4 used in step (a) comprises a molar amount of H 2 SO 4 of from about 1.8 to about 2.5 times the molar amount of chloride in the chloride-containing iron oxide.
Claim 5
Dependent Claim
38 words
The process as described in claim 2, wherein in step (a) the iron oxide is mixed with said solution comprising H 2 SO 4 for a period of time ranging from about 1 minute to about 48 hours.
Claim 6
Dependent Claim
46 words
The process as described in claim 1, wherein the iron oxide separated from step (b) is further heated at a temperature ranging from about 1° C. above ambient temperature to about 1400° C. for a period of time from about 1 minute to about 100 hours.
Claim 7
Dependent Claim
44 words
The process as described in claim 1, wherein the iron oxide separated from step (b) is further heated at a temperature ranging from about 50° C. to about 300° C. for a period of time ranging from about 2 minutes to about one hour.
Claim 8
Dependent Claim
86 words
The process as described in claim 1, wherein the iron oxide separated from step (b) is first heated at a temperature from about 50° C. to about 300° C. for a period of time ranging from about 1 minute to about 72 hours, and the iron oxide is thereafter heated at a temperature from about 400° C. to about 1400° C. at a pressure from about 0.1 atm to about 10 atm for a period of time ranging from about 1 minute to about 72 hours.
Claim 9
Dependent Claim
131 words
A process for removing chloride from a chloride-containing iron oxide, which process comprises the steps of: (a) mixing the chloride-containing iron oxide with an aqueous solution comprising a molar amount of H 2 SO 4 of from about 0.5 to about 5 times the molar amount of chloride present in the chloride-containing iron oxide for a period of time from about 1 minute to about 48 hours to form a mixture; (b) separating the iron oxide from said mixture formed in step (a); and (c) heating the separated iron oxide from step (b) at a temperature from about 1° C. above ambient temperature to about 14000° C. at a pressure from about 0.1 atm to about 10 atm for a period of time from about 1 minute to about 100 hours.
Claim 10
Dependent Claim
131 words
A process for removing chloride from a chloride-containing iron oxide, which process comprises the steps of: (a) mixing the chloride-containing iron oxide with an aqueous solution comprising a molar amount of H 2 SO 4 of from about 0.5 to about 5 times the molar amount of chloride present in the chloride-containing iron oxide for a period of time from about 1 minute to about 48 hours to form a mixture; (b) separating the iron oxide from said mixture formed in step (a); and (c) heating the separated iron oxide from step (b) at a temperature from about 1° C. above ambient temperature to about 14000° C. at a pressure from about 0.1 atm to about 10 atm for a period of time from about 1 minute to about 100 hours.
Claim 11
Dependent Claim
91 words
The process as claimed in claim 8, wherein the solution comprising H 2 SO 4 in step (a) comprises from a molar amount of H 2 SO 4 of from about 0.5 to about 2.5 times the molar amount of chloride present in the chloride-containing iron oxide prior to being mixed with said solution comprising H 2 SO 4 ; wherein in step (a) the iron oxide is mixed with said solution comprising H 2 SO 4 for a period of time ranging from about 3 minutes to about 5 hours.
Claim 12
Dependent Claim
91 words
The process as claimed in claim 8, wherein in step (c) the iron oxide is first heated at a temperature from about 100° C. to about 300° C. at a pressure from about 0.1 atm to about 10 atm for a period of time ranging from about 1 minute to about 72 hours and then heated to a temperature from about 400° C. to about 1400° C. at a pressure from about 0.1 atm to about 10 atm for a period of time from about 1 minute to about 72 hours.
Claim 13
Dependent Claim
168 words
A process for removing chloride from a regenerated iron oxide comprising from about 800 to about 5000 ppm by weight of chloride, wherein said regenerated iron oxide is produced from a hydrochloric acid waste liquid generated from steel pickling, which process comprises the steps of: (a) mixing the regenerated iron oxide with an aqueous solution comprising a molar amount of H 2 SO 4 of from about 0.5 to about 5 times the molar amount of chloride in the regenerated iron oxide for a period of time ranging from about 1 minute to about 48 hours at a pressure from about 0.5 atm to about 100 atm to form a mixture; (b) separating the iron oxide from said mixture formed in step (a); and (c) heating the separated iron oxide from (b) at a temperature ranging from about 100° C. to about 1400° C. at a pressure from about 0.1 atm to about 10 atm for a period of time from about 1 minute to about 72 hours.
Claim 14
Dependent Claim
168 words
A process for removing chloride from a regenerated iron oxide comprising from about 800 to about 5000 ppm by weight of chloride, wherein said regenerated iron oxide is produced from a hydrochloric acid waste liquid generated from steel pickling, which process comprises the steps of: (a) mixing the regenerated iron oxide with an aqueous solution comprising a molar amount of H 2 SO 4 of from about 0.5 to about 5 times the molar amount of chloride in the regenerated iron oxide for a period of time ranging from about 1 minute to about 48 hours at a pressure from about 0.5 atm to about 100 atm to form a mixture; (b) separating the iron oxide from said mixture formed in step (a); and (c) heating the separated iron oxide from (b) at a temperature ranging from about 100° C. to about 1400° C. at a pressure from about 0.1 atm to about 10 atm for a period of time from about 1 minute to about 72 hours.
Claim 15
Dependent Claim
85 words
The process as described in claim 11, wherein in step (c) the iron oxide is first heated at a temperature ranging from about 100° C. to about 300° C. for a period of time ranging from about 1 minute to about 72 hours, and the iron oxide is thereafter heated at a temperature from about 400° C. to about 1400° C. at a pressure from about 0.1 atm to about 10 atm for a period of time from about 1 minute to about 72 hours.
Claim 16
Dependent Claim
47 words
The process as described in claim 11, wherein in step (a) the iron oxide is treated with an aqueous solution comprising a molar amount of H 2 SO 4 of from about 0.5 to about 2.5 times the molar amount of chloride in the regenerated iron oxide.
Claim 17
Dependent Claim
49 words
The process as described in claim 11, wherein, in step (c) the iron oxide is heated at about 700° C. to about 1000° C. at a pressure from about 0.1 atm to about 10 atm for a period of time ranging from about 30 minutes to about 1.5 hours.
Claim 18
Dependent Claim
20 words
The process as described in claim 14, wherein the heating in step (c) is conducted in an oxygen-containing gaseous stream.
Claim 19
Dependent Claim
20 words
The process as described in claim 15, wherein the mixing in step (a) is conducted in an oxygen-containing gaseous stream.
Claim 20
Dependent Claim
20 words
The process as described in claim 14, wherein the heating in step (c) is conducted in air under ambient pressure.
Claim 21
Dependent Claim
20 words
The process as described in claim 15, wherein the mixing in step (a) is conducted in air under ambient pressure.
Claim 22
Dependent Claim
47 words
The process as described in claim 18, wherein the aqueous solution comprising H 2 SO 4 used in step (a) comprises a molar amount of H 2 SO 4 of from about 1.8 to about 2.5 times the molar amount of chloride in the regenerated iron oxide.
References Cited (Backward Citations)
US495197A
Cited
US887042A
Cited
US1837709A
Cited
US2105670A
Cited
US3635664A
Cited
US4092401A
Cited
US4219354A
Cited
US4289746A
Cited
US4452762A
Cited
US4355005A
Cited
JPS5950028A
Cited
JPS5950031A
Cited
US4565675A
Cited
JPS61146719A
Cited
US4701221A
Cited
JPS63112425A
Cited
US4935219A
Cited
JPS63222019A
Cited
JPH01192730A
Cited
JPH03131524A
Cited
US5190906A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1998-03-27 | 1998-09-26 | 1999-03-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2002-03-27 | 2002-09-26 | 2003-03-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2006-03-27 | 2006-09-26 | 2007-03-28 | $7700.00 | Window Closed / Lapsed |