US4288411A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the selective production of a plurality of individual pure halides and/or halide mixtures from a mixture of solid oxides
Assignee: Individual
•
Filing: 1979-08-03
•
Granted: 1981-09-08
•
Expires: 1999-08-03
Abstract
Abstract The process is based on the series of halide-forming affinities. The oxides are passed through a series of zones equal in number to the plurality of halides or mixtures which are to be produced. A halide of an element of lower halide-forming affinity is fed counter-current to the oxides. The halide supply is in stoichiometric equivalent to the total content of halide to be extracted. The oxide of the said fed element is also extracted.
Inventors
- 👤 Gerhard Holland
- 👤 Rudolf Nowak
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 11:26
CPC Classifications
C; C22; C22B; C22B9/00; C22B9/02; C01; C01G; C01G1/00; C01G1/06; C22B1/00; C22B1/02; C22B1/08; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
309 words
A process for the selective production of individual pure halides and/or mixtures of halides from a mixture of solid oxides, either without or with only one single reducing halogenation stage using the known series of halide-forming affinities, characterised by the following features: (a) the comminuted mixture of solid oxides is loaded into the front end of a unit having as many zones as the number of halides or halide mixtures to be produced, and is passed through it; (b) into the rear end of the unit is fed a halide of an element with a lower halide-forming affinity than that of the lowest halide-forming affinity of those to be produced, whereby the quantity of halide supplied is equivalent to the total halogen content of the halides to be extracted from the units; (c) the halide fed into the rear end of the unit and the solid oxide or mixture of oxides arriving there are converted by oxygen-halogen exchange to a solid oxide and a gaseous halide or mixture of halides; (d) the solid oxide formed in the rear end of the unit is separated from the halide or mixture of halides and is removed from the unit; (e) the gaseous halide or mixture of halides formed in the rear end of the unit is brought in contact in counter-current flow with the solid oxide mixture further to the front of the unit whereby again through an oxygen-halogen exchange an individual gaseous halide or mixture of halides is formed in each zone of the unit; and (f) fractions of the gaseous halides or mixtures of halides formed in the individual zones are separated from the solid oxides and extracted from the unit in quantities such that the extracted amount of halide of each element is equivalent to the amount of oxide mixture loaded into the front end of the unit.
Claim 2
Dependent Claim
309 words
A process for the selective production of individual pure halides and/or mixtures of halides from a mixture of solid oxides, either without or with only one single reducing halogenation stage using the known series of halide-forming affinities, characterised by the following features: (a) the comminuted mixture of solid oxides is loaded into the front end of a unit having as many zones as the number of halides or halide mixtures to be produced, and is passed through it; (b) into the rear end of the unit is fed a halide of an element with a lower halide-forming affinity than that of the lowest halide-forming affinity of those to be produced, whereby the quantity of halide supplied is equivalent to the total halogen content of the halides to be extracted from the units; (c) the halide fed into the rear end of the unit and the solid oxide or mixture of oxides arriving there are converted by oxygen-halogen exchange to a solid oxide and a gaseous halide or mixture of halides; (d) the solid oxide formed in the rear end of the unit is separated from the halide or mixture of halides and is removed from the unit; (e) the gaseous halide or mixture of halides formed in the rear end of the unit is brought in contact in counter-current flow with the solid oxide mixture further to the front of the unit whereby again through an oxygen-halogen exchange an individual gaseous halide or mixture of halides is formed in each zone of the unit; and (f) fractions of the gaseous halides or mixtures of halides formed in the individual zones are separated from the solid oxides and extracted from the unit in quantities such that the extracted amount of halide of each element is equivalent to the amount of oxide mixture loaded into the front end of the unit.
Claim 3
Dependent Claim
54 words
A process as claimed in claim 1, whereby the oxide removed from the rear end of the unit is subjected to a reducing halogenation with a halogen or halogen-containing gases or halogen-releasing compounds, and the halide formed is separated from the resulting gaseous mixture and is reintroduced into the rear end of the unit.
Claim 4
Dependent Claim
32 words
A process as claimed in claim 1 whereby the halide or mixture of halides to be produced is separated from the gaseous mixture extracted from a zone, by fractional condensation or distillation.
Claim 5
Dependent Claim
40 words
A process as claimed in claim 1 whereby the halide or mixture of halides to be produced is separated in a known manner from the gaseous mixture extracted from a zone, and the residual waste is reintroduced into the unit.
Claim 6
Dependent Claim
172 words
A process as claimed in claim 1 characterised by the following features: (a) instead of a halide, a reducing agent and a halogen or halogen-containing gas or halogen-releasing compound are fed into the rear end of the unit in quantities equivalent to the total halogen content of the halides extracted from the unit; (b) reducing agent and halogen are converted by the oxide or mixture of oxides arriving at the rear end of the unit to a gaseous halide-containing mixture which is reacted in counter-current flow with the mixture of oxides loaded into the unit; (c) fractions of the halide-containing gaseous mixtures present in the individual zones are separated from the oxides and are extracted from the respective zones in quantities such that the quantities of the halides of every element contained in the gaseous mixtures are equivalent to the quantities of their oxides loaded into the front end of the Unit; (d) the halides are separated from the gaseous mixture extracted from each individual zone and thus freed from the oxides.
Claim 7
Dependent Claim
30 words
A process as claimed in claim 5, whereby the halide or mixture of halides contained in the gaseous mixture extracted from a zone is separated by fractional condensation or distillation.
Claim 8
Dependent Claim
38 words
A process as claimed in claim 5 whereby the halide or mixture of halides contained in the gaseous mixture extracted from a zone is separated in a known manner and the residual gas is reintroduced into the unit.
Claim 9
Dependent Claim
47 words
A process as claimed in claim 1 whereby appropriate quantities of materials having at least no deleterious effect on the chemistry of the process are introduced at corresponding temperatures through suitable points of access to the unit for the purpose of controlling the temperature of the reactions.
Claim 10
Dependent Claim
47 words
A process as claimed in claim 5 whereby appropriate quantities of materials having at least no deleterious effect on the chemistry of the process are introduced at corresponding temperatures through suitable points of access to the unit for the purpose of controlling the temperature of the reactions.
Claim 11
Dependent Claim
24 words
A process as claimed in claim 8 whereby solid or liquid matter is introduced into the unit thereby absorbing heat by melting and/or evaporating.
Claim 12
Dependent Claim
24 words
A process as claimed in claim 9 whereby solid or liquid matter is introduced into the unit thereby absorbing heat by melting and/or evaporating.
Claim 13
Dependent Claim
24 words
A process as claimed in claim 8 whereby gaseous or liquid matter is introduced into the unit thereby releasing heat by condensing and/or solidifying.
Claim 14
Dependent Claim
24 words
A process as claimed in claim 9 whereby gaseous or liquid matter is introduced into the unit thereby releasing heat by condensing and/or solidifying.
Claim 15
Dependent Claim
23 words
A process as claimed in claim 8 whereby the materials used for temperature control are taken from the output of the entire process.
Claim 16
Dependent Claim
23 words
A process as claimed in claim 9 whereby the materials used for temperature control are taken from the output of the entire process.
Claim 17
Dependent Claim
76 words
A process as claimed in claim 5 whereby the halide or mixture of halides contained in a fraction of the gaseous mixture extracted from a zone is separated and the residual gaseous waste is returned to the next zone of the unit where it rejoins the gaseous mixture in the zone, and in which the temperature and quantity of waste gas returned is regulated so that the required reaction temperature is obtained in the next zone.
Claim 18
Dependent Claim
24 words
A process as claimed in claim 16 whereby the returned waste gases are reheated by a hot gaseous mixture extracted from the halogenation vessel.
References Cited (Backward Citations)
US2733983A
Cited
US2758019A
Cited
US3244509A
Cited
US3466169A
Cited
US3853541A
Cited
US4096234A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-09-07 | 1985-03-09 | 1985-09-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-09-07 | 1989-03-09 | 1989-09-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-09-07 | 1993-03-09 | 1993-09-08 | $7700.00 | Window Closed / Lapsed |