Solar desalination system
10183233 ยท 2019-01-22
Assignee
Inventors
Cpc classification
Y02A20/212
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
Y02A20/142
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
Y02A20/124
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
B01D3/00
PERFORMING OPERATIONS; TRANSPORTING
B01D5/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The solar desalination system is a hybrid system combining a Fresnel solar concentrator with a solar desalination still. The solar still includes an absorber base, at least one sidewall, and a hollow cover. The hollow cover has an inlet port for receiving seawater such that the seawater passes through an interior of the hollow cover and exits through at least one outlet port into an open interior region of the solar still. At least one collection duct is secured to an inner face of the at least one sidewall for collecting pure water condensate. A vacuum pump is in communication with the open interior region of the solar still through a vacuum port for selectively lowering the pressure within the open interior region of the solar still. The solar still is suspended above a linear Fresnel reflector array such that the absorber base is positioned at a focal point thereof.
Claims
1. A solar desalination system in which fresh water is derived from seawater, comprising: a stationary solar still consisting of: an absorber base having opposed upper and lower surfaces; at least one sidewall having opposed upper and lower edges, the lower edge thereof being secured to the upper surface of the absorber base, the least one sidewall having a vacuum port and at least one condensate retrieval port; a hollow cover secured to and covering the upper edge of the at least one sidewall, the hollow cover having an inlet port for receiving seawater such that the seawater passes through the hollow cover, the hollow cover having at least one outlet port, the absorber base, at least one sidewall, and hollow cover defining an open interior region; at least one collection duct secured to an inner face of the at least one sidewall for collecting pure water condensate, the at least one collection duct being in fluid communication with the at least one condensate retrieval port; a distribution conduit in direct fluid communication with the at least one outlet port for transferring the seawater from the hollow cover to the open interior region of the solar still; and a condensate retrieval conduit in direct fluid communication with the at least one condensate retrieval port for extracting the pure water condensate; a vacuum pump in direct fluid communication with the open interior region of the solar still through the vacuum port for selectively lowering the pressure within the open interior region of the solar still, wherein the lower pressure within the solar still decreases the boiling temperature of the seawater to below 100 C., thus increasing the evaporation rate of the seawater through the combination of high temperature and lowered boiling point; and a linear Fresnel reflector array, the solar still being suspended above the linear Fresnel reflector array such that the lower surface of the absorber base is positioned at a focal line of the array.
2. The solar desalination system as recited in claim 1, further comprising a closed, optically transparent housing secured to and covering the lower surface of the absorber base.
3. The solar desalination system as recited in claim 2, wherein a vacuum is formed between the closed, optically transparent housing and the lower surface of the absorber base.
4. The solar desalination system as recited in claim 1, further comprising: a seawater tank adapted for holding seawater; and a first pump selectively transferring the seawater from the seawater tank to the interior of the hollow cover through the inlet port.
5. The solar desalination system as recited in claim 4, further comprising: a pure water tank adapted for receiving the pure water condensate; and a second pump selectively transferring the pure water condensate to the pure water tank from the at least one condensate retrieval port through the condensate retrieval conduit.
6. The solar desalination system as recited in claim 1, wherein the hollow cover has an inverted substantially V-shaped cross-section such that the hollow cover has a central apex and a pair of lower edges.
7. The solar desalination system as recited in claim 6, wherein the at least one collection duct comprises a pair of collection ducts respectively positioned adjacent the pair of lower edges of the hollow cover.
8. The solar desalination system as recited in claim 7, wherein the at least one outlet port comprises a pair of outlet ports.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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(7) Similar reference characters denote corresponding features consistently throughout the attached drawings.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
(8) The solar desalination system 10 is a hybrid system, combining a Fresnel solar concentrator with a solar desalination still. As best seen in
(9) In
(10) As shown in
(11) At least one collection duct 40 is secured to an inner face of the at least one sidewall 38 for collecting pure water condensate. The at least one collection duct 40 is in fluid communication with the at least one condensate retrieval port 78. As shown in
(12) As shown in
(13) As shown in
(14) As shown in
(15) A vacuum pump 42 is in fluid communication with the open interior region of the solar still 14 through the vacuum port 46 (via vacuum conduit 44) for selectively lowering the pressure within the open interior region of the solar still 14, thus increasing the rate of evaporation of the seawater. Linear Fresnel reflector arrays can generate temperatures well above 100 C. However, the vacuum pump 42, by lowering the pressure within the solar still 14, can decrease the boiling temperature of water to below 100 C., thus greatly increasing the evaporation rate of the seawater through the combination of high temperature and lowered boiling point. Additionally, as the seawater passes through the hollow cover 30, the seawater not only lowers the temperature of the hollow cover 30 (thus allowing the water vapor to condense on its inner surface) but, through heat exchange with the water vapor, the seawater increases in temperature. Thus, the seawater is preheated by this heat exchange process before being heated by the concentrated solar radiation S and having its boiling point lowered by operation of the vacuum pump 42.
(16) Further, a closed, optically transparent housing 36 may be secured to and cover the lower surface 72 of the absorber base 34 to prevent heat loss from the absorber base 34 through convective heat transfer with the ambient environment. A vacuum may be formed within the closed, optically transparent housing 36 to further enhance the thermal insulation. In
(17) It is to be understood that the solar desalination system is not limited to the specific embodiments described above, but encompasses any and all embodiments within the scope of the generic language of the following claims enabled by the embodiments described herein, or otherwise shown in the drawings or described above in terms sufficient to enable one of ordinary skill in the art to make and use the claimed subject matter.