US4239515A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Gas-liquid contact reaction apparatus
Assignee: Chiyoda Corp
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Filing: 1979-02-09
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Granted: 1980-12-16
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Expires: 1999-02-09
Abstract
Abstract An improved compact apparatus for gas-liquid contact and separation by precipitation of solids therein, which essentially comprises a splash separating section, a solid-gas-liquid contact section and a solid depositing section formed in a single reaction vessel, in which gas is blown into the vessel through a gas disperser having a gas outlet opened below the liquid surface in said solid-gas-liquid contact section and caused to undergo contact with the phase of a suspension forcibly circulated from said solid depositing section formed below said solid-gas-liquid contact section, whereby the precipitated solids are prevented from depositing the inner surface of the vessel and other attendant members.
Inventors
- 👤 Hiroshi Yanagioka
- 👤 Atsushi Futami
- 👤 Masatake Shinsenji
- 👤 Minoru Tanaka
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 09:10
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501; B01D53/504; C; C01; C01C; C01C1/00; C01C1/24; C01C1/242; C01D; C01D7/00; C01D7/18
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
403 words
Gas-liquid contact reaction apparatus comprising a vessel having a liquid therein, said vessel being provided with funnel-shaped gas introducing means extending from the top of the vessel downwardly to a substantially central portion of the vessel, said gas introducing means having at its lower open end a flared skirt-like perforated gas dispersing means and a non-perforated side wall member disposed around the lower end periphery of said gas dispersing means, said gas dispersing means being disposed completely below the liquid level and adapted to form above the same a froth layer of a mixture of a solid, liquid and gas, whereby when gas is introduced into the vessel there is formed in the vessel a splash separating section above said froth layer of a solid, liquid and gas mixture, an intermediate solid-gas-liquid contact section including said froth layer, and a lower solid precipitating section below said froth layer, said splash separating section including means comprising a space for separating gas from a splash liquid and a gas outlet for allowing gas to flow from said space, said solid-gas-liquid contact section including means positioned below and contiguous with said splash separating section comprising a lower end portion of said gas introducing means introducing the gas into the end portion for dispersing the gas through said skirt-like perforated gas dispersing means, for preventing the gas from escaping by the side wall member and for compressing the liquid beneath said gas dispersing means, such that the level of the liquid beneath the gas dispersing means is lower than the level of the liquid in said solid-gas-liquid contact section and wherein a space is formed between said gas dispersing means and the level of the liquid below the gas dispersing means, said gas dispersing means being positioned with respect to said gas introducing means such that the gas is forced to bubble up through the gas dispersing means to rise through the liquid in the solid-gas-liquid contact section and wherein the solids are introduced into the end portion together with the gas through the open bottom below said gas dispersing means, thus avoiding plugging of the gas dispersing means, and said solid precipitating section is positioned below and contiguous with said contact section and has a stirrer and an air introducing means therein for forming a suspension containing solid particles and for causing circulation, thereby making an exchange between a mixture of solid, gas and liquid thereabove.
Claim 2
Dependent Claim
403 words
Gas-liquid contact reaction apparatus comprising a vessel having a liquid therein, said vessel being provided with funnel-shaped gas introducing means extending from the top of the vessel downwardly to a substantially central portion of the vessel, said gas introducing means having at its lower open end a flared skirt-like perforated gas dispersing means and a non-perforated side wall member disposed around the lower end periphery of said gas dispersing means, said gas dispersing means being disposed completely below the liquid level and adapted to form above the same a froth layer of a mixture of a solid, liquid and gas, whereby when gas is introduced into the vessel there is formed in the vessel a splash separating section above said froth layer of a solid, liquid and gas mixture, an intermediate solid-gas-liquid contact section including said froth layer, and a lower solid precipitating section below said froth layer, said splash separating section including means comprising a space for separating gas from a splash liquid and a gas outlet for allowing gas to flow from said space, said solid-gas-liquid contact section including means positioned below and contiguous with said splash separating section comprising a lower end portion of said gas introducing means introducing the gas into the end portion for dispersing the gas through said skirt-like perforated gas dispersing means, for preventing the gas from escaping by the side wall member and for compressing the liquid beneath said gas dispersing means, such that the level of the liquid beneath the gas dispersing means is lower than the level of the liquid in said solid-gas-liquid contact section and wherein a space is formed between said gas dispersing means and the level of the liquid below the gas dispersing means, said gas dispersing means being positioned with respect to said gas introducing means such that the gas is forced to bubble up through the gas dispersing means to rise through the liquid in the solid-gas-liquid contact section and wherein the solids are introduced into the end portion together with the gas through the open bottom below said gas dispersing means, thus avoiding plugging of the gas dispersing means, and said solid precipitating section is positioned below and contiguous with said contact section and has a stirrer and an air introducing means therein for forming a suspension containing solid particles and for causing circulation, thereby making an exchange between a mixture of solid, gas and liquid thereabove.
Claim 3
Dependent Claim
51 words
Apparatus as defined in claim 1 further comprising liquid supply means on top of the inner wall of the gas introducing means for supplying a stream of liquid as a wet film over the inner wall of said gas introducing means for preventing deposition of any solids on said inner wall.
Claim 4
Dependent Claim
32 words
Apparatus as defined in claim 6 wherein said gas dispersing means comprises a gas bubble producer selected from the group consisting of a perforated plate a net, a grid or a screen.
Claim 5
Dependent Claim
22 words
Apparatus as defined in claim 1, wherein said reaction vessel includes downtakes connecting said solid-gas-liquid contact section and said solid precipitating section.
Claim 6
Dependent Claim
18 words
Apparatus as defined in claim 1, wherein a baffle is provided surrounding said stirrer and air introducing means.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-12-16 | 1984-06-16 | 1984-12-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-12-16 | 1988-06-16 | 1988-12-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-12-16 | 1992-06-16 | 1992-12-16 | $7700.00 | Window Closed / Lapsed |