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Hydrate-based desalination with hydrate-elevating density-driven circulation

a technology of density-driven circulation and desalination, which is applied in the direction of vacuum distillation separation, separation process, vessel construction, etc., to achieve the effect of increasing the rate at which hydrates, improving heat dissipation, and more hydrates

Inactive Publication Date: 2005-11-10
WATER REGENERATION SYST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

"The invention is a method for conducting hydrate-based desalination or water purification in a hydrate fractionation column. The method involves introducing hydrate-forming substance into the column and allowing the hydrate to rise naturally through the column. The hydrate is then dissociated to release fresh or purified water and the hydrate-forming substance. The released water is reintroduced into the column at a lower region, where it mixes with the hydrate and flows upward through the column. This circulation pattern enhances the rate at which the hydrate rises, improving the yield of fresh water and minimizing the mixing of residual brine. The use of smaller hydrate masses also reduces the required residence time and improves heat dissipation. The invention helps prevent seawater and residual brines from being drawn upward with the hydrate as it rises, resulting in better desalination efficiency."

Problems solved by technology

As the hydrate rises, it becomes unstable and disassociates into pure water and the hydrate-forming gas or gas mixture.

Method used

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  • Hydrate-based desalination with hydrate-elevating density-driven circulation
  • Hydrate-based desalination with hydrate-elevating density-driven circulation
  • Hydrate-based desalination with hydrate-elevating density-driven circulation

Examples

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Embodiment Construction

[0025] A land-based desalination installation is shown schematically in FIG. 1 in generalized fashion. The installation may be divided roughly into three sections or regions: an intake portion 10; a water purification portion 12; and post-processing and downstream usage section 14.

[0026] The intake portion 10 consists essentially of the apparatus and various subinstallations necessary to extract seawater from the ocean 16 and transport it to the desalination / purification installation at region 12, including subaquatic water intake piping 18 and pumping means (not shown) to draw the water from the ocean and pump it to shore for subsequent processing. Large volume installations can be located relatively close to the sea to reduce the piping distance of the input water to a minimum, and establishing the installation as close to sea level as possible will reduce the cost of pumping against pressure head.

[0027] The intake pipeline 18 preferably extends sufficiently out to sea that it d...

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Abstract

In hydrate-based desalination or other water purification conducted using naturally buoyant or trapped-gas-assisted buoyancy hydrate in a hydrate fractionation column, a portion of fresh or purified product water is extracted from an upper, hydrate dissociation region of the fractionation column and reintroduced into a lower portion of the fractionation column at a point above but generally near a product water / saline water interface. The difference in density between the reintroduced product water and the fluid in the hydrate fractionation column above the point of reintroduction (water, hydrate, and gas) drives a natural circulation system which enhances the rate at which hydrate rises into the hydrate dissociation region.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS [0001] This application is a continuation-in-part of co-pending U.S. patent application Ser. No. 10 / 266,258 filed Oct. 8, 2002, which is a divisional of U.S. patent application Ser. No. 09 / 397,500 filed Sep. 17, 1999 (now issued as U.S. Pat. No. 6,497,794 on Dec. 24, 2002), which is a continuation-in-part of U.S. patent application Ser. No. 09 / 375,410 filed Aug. 17, 1999 (now issued as U.S. Pat. No. 6,531,034 on Mar. 11, 2003), which is a continuation-in-part of U.S. patent application Ser. No. 09 / 350,906 filed on Jul. 12, 1999 (now issued as U.S. Pat. No. 6,565,715 on May 20, 2003), the entire contents of all four of which are incorporated by reference. Priority is claimed from each of those four applications. [0002] This application is also a continuation-in-part of co-pending U.S. patent application Ser. No. 09 / 941,545 filed Aug. 30, 2001, which is based on now-expired provisional U.S. Patent Application Ser. Nos. 60 / 230,790 filed Sep. 7, 2...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C02F1/00C02F1/04C02F1/22
CPCC02F1/22C02F2103/08C02F1/26Y02A20/124
Inventor MAX, MICHAEL D.KORSGAARD, JENS
Owner WATER REGENERATION SYST
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