US4686009A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Distillation system
Assignee: LANEY JAMES W SUNRAY
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Filing: 1985-10-29
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Granted: 1987-08-11
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Expires: 2005-10-29
Abstract
Abstract A vacuum distillation system uses a tower having an open bottom submerged within a tank of solution exposed to atmospheric pressure. The solution within the tower is elevated to barometric level by a high vacuum or low absolute pressure on the tower top. As solution flows through the open bottom and upward, the solution is heated and then cooled to cause degasification and precipitation, and then withdrawn from the tower top. The treated solution is flowed to a vaporization chamber that is subjected to a low absolute pressure. A heater maintains the solution at a selected chamber temperature above the boiling point of water at the selected chamber pressure. The chamber pressure and temperature may be selected as desired to yield the purest water distillate for almost any solution of water and impurities. Water vapor is pumped from the vaporization chamber by a vapor pump to a condenser, where condensation results from increased pressure and decreased temperature. The distillate water is removed from the condenser by a pump to a storage tank. The storage tank is also maintained under vacuum to keep the water gas free.
Inventors
- 👤 Derald L. McCabe
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 21:29
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/04; B01D3/10; B01D5/00; B01D5/0003; B01D5/0012; B01D5/0033; B01D5/0045; B01D5/0057; B01D5/006; B01D5/0069; Y; Y10; Y10S; Y10S159/00; Y10S159/02; Y10S159/16; Y10S203/00; Y10S203/09; Y10S203/11
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
385 words
Apparatus for water distillation comprising: a. means defining a source of solution that includes water, b. a supply tank, c. a supply line connecting the source of solution to the supply tank, d. a supply control means connected to the supply line for maintaining a supply level of the solution within the supply tank, e. a vent means connected to the supply tank, f. a degasification tower having sides, a top, and a bottom, said tower extending from above the supply tank to below the supply level within the supply tank, g. a vacuum pump means connected to the degasification tower proximate the tower top for maintaining a tower gas pressure substantially below atmospheric pressure, h. a lower heat exchanger in the tower, proximate the bottom of the tower, for adding heat to solution within the tower, i. an upper heat exchanger within the tower proximate the top of the tower for removing sufficient heat from the solution so that the temperature of the solution above the upper heat exchanger is below the boiling point of water at the tower gas pressure, j. a vaporization chamber, k. a chamber line connecting the vaporization chamber to the degasification tower, l. a level control means connected to the chamber line for maintaining a chamber level of the solution within the said chamber, m. a heater means connected to the vaporization chamber for maintaining the solution within the vaporization chamber at a chamber temperature that is substantially below the atmospheric boiling point of water, n. a condenser vessel, o. a vapor duct connecting the vaporization chamber to the condenser vessel, p. a vapor pump connected to the vapor duct for transferring water vapor from the vaporization chamber to the condenser through the vapor duct: and for maintaining a chamber gas pressure in the vaporization chamber that is substantially below atmospheric pressure, q. a cooling means connected to the condenser vessel for cooling the water vapor; r. a closed storage tank, s. a storage line connecting the storage tank with the condenser vessel at a bottom of the condenser vessel, t. a vacuum valve connected to the storage tank for maintaining a storage gas pressure within the storage tank that is less than atmospheric pressure and greater than the vaporization chamber gas pressure and the degasification tower gas pressure.
Claim 2
Dependent Claim
385 words
Apparatus for water distillation comprising: a. means defining a source of solution that includes water, b. a supply tank, c. a supply line connecting the source of solution to the supply tank, d. a supply control means connected to the supply line for maintaining a supply level of the solution within the supply tank, e. a vent means connected to the supply tank, f. a degasification tower having sides, a top, and a bottom, said tower extending from above the supply tank to below the supply level within the supply tank, g. a vacuum pump means connected to the degasification tower proximate the tower top for maintaining a tower gas pressure substantially below atmospheric pressure, h. a lower heat exchanger in the tower, proximate the bottom of the tower, for adding heat to solution within the tower, i. an upper heat exchanger within the tower proximate the top of the tower for removing sufficient heat from the solution so that the temperature of the solution above the upper heat exchanger is below the boiling point of water at the tower gas pressure, j. a vaporization chamber, k. a chamber line connecting the vaporization chamber to the degasification tower, l. a level control means connected to the chamber line for maintaining a chamber level of the solution within the said chamber, m. a heater means connected to the vaporization chamber for maintaining the solution within the vaporization chamber at a chamber temperature that is substantially below the atmospheric boiling point of water, n. a condenser vessel, o. a vapor duct connecting the vaporization chamber to the condenser vessel, p. a vapor pump connected to the vapor duct for transferring water vapor from the vaporization chamber to the condenser through the vapor duct: and for maintaining a chamber gas pressure in the vaporization chamber that is substantially below atmospheric pressure, q. a cooling means connected to the condenser vessel for cooling the water vapor; r. a closed storage tank, s. a storage line connecting the storage tank with the condenser vessel at a bottom of the condenser vessel, t. a vacuum valve connected to the storage tank for maintaining a storage gas pressure within the storage tank that is less than atmospheric pressure and greater than the vaporization chamber gas pressure and the degasification tower gas pressure.
Claim 3
Dependent Claim
22 words
The apparatus as defined in claim 1 further comprising: a plurality of baffles disposed within the vaporization chamber for trapping water droplets.
Claim 4
Dependent Claim
34 words
The apparatus as defined in claim 1 further comprising: a float means at the top of the tower, and means for spacing an end of the chamber line below the surfaces of the solution.
Claim 5
Dependent Claim
54 words
The apparatus as defined in claim 1: wherein said heater means includes a heat exchanger having a heater shell, a heat source connected to the shell for heating the solution within, and heater exchanger tubes disposed within the heater shell; and wherein the condenser vessel includes a condenser exchanger tubes disposed within said condenser.
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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) | 1990-08-10 | 1991-02-09 | 1991-08-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-08-10 | 1995-02-09 | 1995-08-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-08-10 | 1999-02-09 | 1999-08-11 | $7700.00 | Window Closed / Lapsed |