US4152218A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for the distillation of sea water
Assignee: Hitachi Ltd
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Filing: 1976-11-10
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Granted: 1979-05-01
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Expires: 1996-11-10
Abstract
Abstract Apparatus for the distillation of sea water and desulfurization has a vessel directly contacting waste gases exhausting from a boiler with sea water for absorbing sulfur oxides contained within the waste gases, an oxidation device to convert the sulfites that are produced by absorption of the sulfur oxide into sulfates through a catalytic action of metallic ions in the sea water, a decarbonization device, a deaerator, and a heating type distillation apparatus that uses the sea water used for the desulfurization as supplementary water. The oxidation, desulfurization and the separation of air are processes conducted continuously.
Inventors
- 👤 Tsuneo Narita
- 👤 Shigeo Yoshihara
- 👤 Yoshihiro Ikenaga
- 👤 Tokuji Iijima, deceased
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 18:11
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/507; C; C02; C02F; C02F1/00; C02F1/02; C02F1/04; C02F1/042; C02F1/06; Y; Y10; Y10S; Y10S203/00; Y10S203/18
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
294 words
A method for the removal of sulfur oxides from the exhaust gases of an industrial source of exhaust gases containing sulfur oxides and for the pretreatment of sea water to be distilled in a heated distillation apparatus for the prevention of scale depositing, comprising the steps of:providing exhaust gases containing sulfur oxide as sulfuric anhydride gases from an industrial source; providing seawater that naturally has alkaline metallic ion; contacting the exhaust gases containing sulfur oxides with the alkaline sea water to absorb the sulfuric anhydride gases of the waste gases into the sea water, in proportions such that the quantity of sulfuric anhydride gases absorbed in the sea water to produce sulfuric anhydride ions dissolved in the sea water does not exceed the equivalence of all the alkaline ions in the sea water and further such that the quantity of sulfuric anhydride gases absorbed in the sea water will substantially completely react with the metallic ions in the sea water to produce metallic sulfites; contacting the sea water having sulfites therein, as produced by the preceeding step, with an oxygen containing gas sufficiently for the metallic sulfites to be transformed to stable metallic sulfates through the catalytic action of the metallic ions in the sea water; decarbonizing the sea water by the carbonic acid ions in the sea water reacting with the hydrogen ions produced by the absorption of the sulfuric anhydride gases to produce water and carbon dioxide that is removed from the solution; and controlling all of the preceding steps so that the thus treated sea water is in the region of alkalinity with stable metallic sulfates and without any substantial amount of sulfuric acid and without any substantial increase in the temperature of the sea water as caused by said steps.
Claim 2
Independent Claim
294 words
A method for the removal of sulfur oxides from the exhaust gases of an industrial source of exhaust gases containing sulfur oxides and for the pretreatment of sea water to be distilled in a heated distillation apparatus for the prevention of scale depositing, comprising the steps of:providing exhaust gases containing sulfur oxide as sulfuric anhydride gases from an industrial source; providing seawater that naturally has alkaline metallic ion; contacting the exhaust gases containing sulfur oxides with the alkaline sea water to absorb the sulfuric anhydride gases of the waste gases into the sea water, in proportions such that the quantity of sulfuric anhydride gases absorbed in the sea water to produce sulfuric anhydride ions dissolved in the sea water does not exceed the equivalence of all the alkaline ions in the sea water and further such that the quantity of sulfuric anhydride gases absorbed in the sea water will substantially completely react with the metallic ions in the sea water to produce metallic sulfites; contacting the sea water having sulfites therein, as produced by the preceeding step, with an oxygen containing gas sufficiently for the metallic sulfites to be transformed to stable metallic sulfates through the catalytic action of the metallic ions in the sea water; decarbonizing the sea water by the carbonic acid ions in the sea water reacting with the hydrogen ions produced by the absorption of the sulfuric anhydride gases to produce water and carbon dioxide that is removed from the solution; and controlling all of the preceding steps so that the thus treated sea water is in the region of alkalinity with stable metallic sulfates and without any substantial amount of sulfuric acid and without any substantial increase in the temperature of the sea water as caused by said steps.
Claim 3
Dependent Claim
78 words
The method of claim 1, wherein all of the industrial source exhaust gas is treated with the sea water to remove substantially all of its sulfur oxides, and thereafter directly discharging the exhaust gases into the atmosphere; and thereafter including the step of feeding the sea water substantially within the alkaline range with stable sulfates to a distillation apparatus according to the capacity of the distillation apparatus and automatically releasing any excess treated sea water to the environment.
Claim 4
Dependent Claim
94 words
The method of claim 2, further including the step of heating the sea water prior to said step of contacting the exhaust gases with the sea water; and wherein said step of feeding feeds sea water substantially within the alkaline range and having stable sulfates to a multistage flash evaporator having a heat recovery section, a heat dissipation section and a final flash chamber, passes fresh sea water through heat exchange tubes of the heat dissipation section as cooling water, and thereafter discharges the cooling water from the heat dissipation section to the environment.
Claim 5
Dependent Claim
39 words
The method of claim 3, further including the step of deaerating the sea water substantially within the alkaline range and with stable sulfates for removing dissolved air and oxygen from the sea water prior to said step of heating.
Claim 6
Dependent Claim
33 words
The method of claim 2, further including the step of deaerating the sea water substantially within the alkaline range and with stable sulfates for removing dissolved air and oxygen from the sea water.
Claim 7
Dependent Claim
33 words
The method of claim 1, further including the step of deaerating the sea water substantially within the alkaline range and with stable sulfates for removing dissolved air and oxygen from the sea water.
Claim 8
Dependent Claim
26 words
The method of claim 1, including the step of heating the sea water prior to said step of contacting the exhaust gases with the sea water.
Claim 9
Dependent Claim
62 words
The method of claim 7, further including the steps of thereafter feeding the sea water substantially within the alkaline range and with stable sulfates to a multistage flash evaporator having a heat recovery section, a heat dissipation section, and a final flash chamber; and passing fresh sea water and thereafter discharging the cooling water from the heat dissipation section to the environment.
Claim 10
Dependent Claim
77 words
The method of claim 1, wherein said step of contacting the sea water with an oxygen containing gas and said step of decarbonizing the sea water are conducted in one common vessel simultaneously by spraying the sea water with absorbed sulfur oxides downwardly from an upper portion of the vessel and forcing air upwardly from a lower portion of the vessel through the downwardly sprayed sea water and in direct contact with the downwardly sprayed sea water.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-04-30 | 1982-10-30 | 1983-05-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-04-30 | 1986-10-30 | 1987-05-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-04-30 | 1990-10-30 | 1991-05-01 | $7700.00 | Window Closed / Lapsed |