Patent US4065271A successfully refreshed from Google Patents.
US4065271A
Expired / Lapsed
US
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Process of separating hydrogen fluoride from gases
Assignee: GEA Group AG
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Filing: 1975-10-10
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Granted: 1977-12-27
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Expires: 1995-10-10
Abstract
Abstract Hydrogen fluoride is removed from gases by introducing the gases into a fluidized-bed reactor to form a gas-solid suspension, entraining a major part of the solids in an upward direction separating the solids entrained by the gases without prior removal of the solids from the gas-solid suspension, by means of an electrostatic precipitator.
Inventors
- 👤 Ernst Weckesser
- 👤 Volker Sparwald
- 👤 Lothar Reh
- 👤 Eberhard Bohm
- 👤 Rolf Graf
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 22:28
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/68
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
249 words
A process for removing hydrogen fluoride from a gas which comprises the combination of the following steps: a. introducing the gas into a fluidized bed reactor at a velocity of 1 to 5m/sec calculated for the empty reactor to form a gas-solid suspension in which the solids concentration decreases from bottom to top and wherein the solids have a particle size of 20 to 300 microns; b. extracting solids from said reactor substantially exclusively in an upward direction by entrainment with gas in a gas-solid suspension having a solids content of the order of 175 to 250 grams per cubic meter (STP) of the extracted suspension; c. separating the solids extracted in step (b) from the entraining gas without prior removal of the solids from the gas-solid suspension which has a dust resistivity adjusted to be below 10 12 Ohm-cm by means of an electrostatic precipitator directly following the reactor and constituting the sole gas/solid separator downstream of the reactor; d. simultaneously with the separation of the solids from the entraining gas classifying the separated particles of the solids in said electrostatic precipitator into fine-grain and coarse-grain fractions; e. recycling the coarse-grain fraction into the fluidized bed reactor to form a circulating fluidized bed therein while discharging the fine-grain fraction upon which impurities in said gas preferentially adsorb; and f. discharging gas from said electrostatic precipitator after the separation of said particles therefrom as an exhaust gas containing at most about 1 mg/m 3 (STP) of fluorine as HF.
Claim 2
Dependent Claim
249 words
A process for removing hydrogen fluoride from a gas which comprises the combination of the following steps: a. introducing the gas into a fluidized bed reactor at a velocity of 1 to 5m/sec calculated for the empty reactor to form a gas-solid suspension in which the solids concentration decreases from bottom to top and wherein the solids have a particle size of 20 to 300 microns; b. extracting solids from said reactor substantially exclusively in an upward direction by entrainment with gas in a gas-solid suspension having a solids content of the order of 175 to 250 grams per cubic meter (STP) of the extracted suspension; c. separating the solids extracted in step (b) from the entraining gas without prior removal of the solids from the gas-solid suspension which has a dust resistivity adjusted to be below 10 12 Ohm-cm by means of an electrostatic precipitator directly following the reactor and constituting the sole gas/solid separator downstream of the reactor; d. simultaneously with the separation of the solids from the entraining gas classifying the separated particles of the solids in said electrostatic precipitator into fine-grain and coarse-grain fractions; e. recycling the coarse-grain fraction into the fluidized bed reactor to form a circulating fluidized bed therein while discharging the fine-grain fraction upon which impurities in said gas preferentially adsorb; and f. discharging gas from said electrostatic precipitator after the separation of said particles therefrom as an exhaust gas containing at most about 1 mg/m 3 (STP) of fluorine as HF.
Claim 3
Dependent Claim
20 words
The process defined in claim 1 wherein the dust resistivity in step (c) is adjusted to below 10 11 Ohm-cm.
Claim 4
Dependent Claim
26 words
The process defined in claim 2 wherein the gas-solid suspension is conditioned for the separation in step (c) by feeding water into the fluidized bed reactor.
Claim 5
Dependent Claim
21 words
The process defined in claim 1 wherein the temperature of the gas-solid suspension in step (a) is 40° to 85° C.
Claim 6
Dependent Claim
32 words
The process defined in claim 1 wherein the gas introduced into said fluidized bed reactor contains hydrogen fluoride and is introduced through at least one venturi inlet into said fluidized bed reactor.
Claim 7
Dependent Claim
28 words
The process defined in claim 1 wherein the resistance time of the solids in said fluidized bed reactor is increased by the incorporation of a baffle separator therein.
Claim 8
Dependent Claim
28 words
The process defined in claim 1 wherein the minimum solids concentration in the fluidized bed reactor is 2 to 10 kg per m 3 of the reactor volume.
References Cited (Backward Citations)
US3477203A
Cited
US3780497A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-12-26 | 1981-06-27 | 1981-12-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-12-26 | 1985-06-27 | 1985-12-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-12-26 | 1989-06-27 | 1989-12-27 | $7700.00 | Window Closed / Lapsed |