US4297332A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for treatment of a discharge liquid produced in treatment of an exhaust gas
Assignee: Mitsubishi Heavy Industries Ltd
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Filing: 1980-01-16
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Granted: 1981-10-27
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Expires: 2000-01-16
Abstract
Abstract A process for treating an exhaust gas discharged from a coal combustion apparatus, in which the exhaust gas is first led to a dry type dust collecting device, and after fly ash in said exhaust gas is removed, said exhaust gas is treated by a wet type exhaust gas cleaning device; a part of said fly ash collected in said dry type dust collecting device is added to a discharge liquid or a discharge sludge discharged from said wet type exhaust gas cleaning device. The amount of the fly ash to be added to the discharge sludge should be at least three times (in weight) as much as the amount of water contained in said discharge sludge. Preferably fly ash of approximately the same weight as that of said discharge sludge should be added to the discharge sludge discharged from said wet type exhaust gas cleaning device, and subsequently calcium hydroxide of about one-tenth in weight of said discharge sludge should be added to the mixture for solidifying said discharge sludge. In a preferred embodiment, the mixture of the discharge liquid and the fly ash is led to a solid-liquid separator to separate the mixture into clear water and sludge, and the clear water is returned to said wet type exhaust gas cleaning device, while the separated sludge is mixed with additional fly ash to further eliminate a discharge water.
Inventors
- 👤 Atsushi Tatani
- 👤 Susumu Okino
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 23:35
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
285 words
In a method for treatment of an exhaust gas which comprises the steps of treating an exhaust gas discharged from a coal combustion apparatus in a dry type dust collecting device to remove fly ash from said exhaust gas, treating the resultant exhaust gas from said dry type dust collecting device in a cooling tower where halogen gas in said exhaust gas is absorbed to produce a liquid containing a halogen compound, treating the exhaust gas from said cooling tower in an absorption tower where SO 2 is absorbed to produce a slurry containing calcium sulfite, oxidizing said slurry containing calcium sulfite into a gypsum slurry, and separating said gypsum slurry into solid and liquid to recover gypsum and at the same time to obtain filtrate separated from said gypsum, the improvement wherein: (1) said dry type dust collecting device is divided into at least two sections along the direction of gas flow to separate the collected fly ash into at least two parts, one part being fly ash collected on the most upstream side of said gas flow, and a second part being fly ash collected on the downstream side of said gas flow; (2) said filtrate separated from said gypsum, and said liquid containing said halogen compound from said cooling tower, are mixed with a part of said fly ash collected at said most upstream side of said gas flow in said dry type dust collecting device to form a mixed slurry; and (3) said mixed slurry is separated into clear water and sludge, said clear water is supplied to said cooling tower, and said sludge is mixed with a part of said fly ash collected in said dry type dust collecting device.
Claim 2
Dependent Claim
285 words
In a method for treatment of an exhaust gas which comprises the steps of treating an exhaust gas discharged from a coal combustion apparatus in a dry type dust collecting device to remove fly ash from said exhaust gas, treating the resultant exhaust gas from said dry type dust collecting device in a cooling tower where halogen gas in said exhaust gas is absorbed to produce a liquid containing a halogen compound, treating the exhaust gas from said cooling tower in an absorption tower where SO 2 is absorbed to produce a slurry containing calcium sulfite, oxidizing said slurry containing calcium sulfite into a gypsum slurry, and separating said gypsum slurry into solid and liquid to recover gypsum and at the same time to obtain filtrate separated from said gypsum, the improvement wherein: (1) said dry type dust collecting device is divided into at least two sections along the direction of gas flow to separate the collected fly ash into at least two parts, one part being fly ash collected on the most upstream side of said gas flow, and a second part being fly ash collected on the downstream side of said gas flow; (2) said filtrate separated from said gypsum, and said liquid containing said halogen compound from said cooling tower, are mixed with a part of said fly ash collected at said most upstream side of said gas flow in said dry type dust collecting device to form a mixed slurry; and (3) said mixed slurry is separated into clear water and sludge, said clear water is supplied to said cooling tower, and said sludge is mixed with a part of said fly ash collected in said dry type dust collecting device.
Claim 3
Dependent Claim
41 words
A method according to claim 1, wherein the amount of said fly ash, collected in said dry type dust collecting device, mixed with said sludge is at least three times by weight of the amount of water contained in said sludge.
Claim 4
Dependent Claim
61 words
A method according to claim 1, wherein the amount of said fly ash, collected in said dry type dust collecting device, mixed with said sludge is substantially equal in weight to the weight of said sludge, and further, calcium hydroxide in an amount of about one-tenth the weight of said sludge is added to said mixture of fly ash and sludge.
Claim 5
Dependent Claim
252 words
In a method for treatment of an exhaust gas which comprises the steps of treating an exhaust gas discharged from a coal combustion apparatus in a dry type dust collecting device to remove fly ash from said exhaust gas, treating the resultant exhaust gas from said dry type dust collecting device in an absorption tower where halogen gas and SO 2 in said exhaust gas are absorbed to produce a slurry containing calcium sulfite, oxidizing said slurry containing calcium sulfite into a gypsum slurry, and separating said gypsum slurry into solid and liquid to recover gypsum and at the same time to obtain filtrate separated from said gypsum, the improvement wherein: (1) said dry type dust collecting device is divided into at least two sections along the direction of gas flow to separate the collected fly ash into at least two parts, one part being fly ash collected on the most upstream side of said gas flow, and a second part being fly ash collected on the downstream side of said gas flow; (2) said filtrate separated from said gypsum is mixed with a part of said fly ash collected at said most upstream side of said gas flow in said dry type dust collecting device to form a mixed slurry; and (3) said mixed slurry is separated into clear water and sludge, said clear water is supplied to said absorption tower, and said sludge is mixed with a part of said fly ash collected in said dry type dust collecting device.
Claim 6
Dependent Claim
252 words
In a method for treatment of an exhaust gas which comprises the steps of treating an exhaust gas discharged from a coal combustion apparatus in a dry type dust collecting device to remove fly ash from said exhaust gas, treating the resultant exhaust gas from said dry type dust collecting device in an absorption tower where halogen gas and SO 2 in said exhaust gas are absorbed to produce a slurry containing calcium sulfite, oxidizing said slurry containing calcium sulfite into a gypsum slurry, and separating said gypsum slurry into solid and liquid to recover gypsum and at the same time to obtain filtrate separated from said gypsum, the improvement wherein: (1) said dry type dust collecting device is divided into at least two sections along the direction of gas flow to separate the collected fly ash into at least two parts, one part being fly ash collected on the most upstream side of said gas flow, and a second part being fly ash collected on the downstream side of said gas flow; (2) said filtrate separated from said gypsum is mixed with a part of said fly ash collected at said most upstream side of said gas flow in said dry type dust collecting device to form a mixed slurry; and (3) said mixed slurry is separated into clear water and sludge, said clear water is supplied to said absorption tower, and said sludge is mixed with a part of said fly ash collected in said dry type dust collecting device.
Claim 7
Dependent Claim
41 words
A method according to claim 4, wherein the amount of said fly ash, collected in said dry type dust collecting device, mixed with said sludge is at least three times by weight of the amount of water contained in said sludge.
Claim 8
Dependent Claim
61 words
A method according to claim 4, wherein the amount of said fly ash, collected in said dry type dust collecting device, mixed with said sludge is substantially equal in weight to the weight of said sludge, and further, calcium hydroxide in an amount of about one-tenth the weight of said sludge is added to said mixture of fly ash and sludge.
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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) | 1984-10-26 | 1985-04-27 | 1985-10-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-10-26 | 1989-04-27 | 1989-10-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-10-26 | 1993-04-27 | 1993-10-27 | $7700.00 | Window Closed / Lapsed |