Brine mining process
US-2016272513-A1 · Sep 22, 2016 · US
US10040533B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10040533-B2 |
| Application number | US-201514740401-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 16, 2015 |
| Priority date | Aug 13, 2014 |
| Publication date | Aug 7, 2018 |
| Grant date | Aug 7, 2018 |
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A ballast water treatment apparatus for a ship includes a water collection part for collecting sea water, a forward osmosis process unit for producing ballast water and treatment water obtained by desalinating the sea water collected through the water collection part, and a ballast water tank for storing the ballast water produced by the forward osmosis process unit. Since the sea water is treated using a forward osmosis process, fresh water required within the ship can be supplied and the treated sea water can be used as ballast water. In addition, since waste heat and carbon dioxide generated in the ship are used to treat the sea water, the ballast water can be treated and produced in a low-cost and high efficient manner.
Opening claim text (preview).
What is claimed is: 1. A ballast water treatment apparatus on a ship, comprising: a water collection part for collecting sea water in the ship; a forward osmosis process unit configured to produce ballast water and fresh water on a ship that is obtained by desalinating the sea water collected through the water collection part; wherein the forward osmosis process unit comprises: a pre-treatment part configured to receive the sea water from the water collection part and produce pre-treated water; a forward osmosis membrane module configured to receive the pre-treated water and to produce a mixture solution by using a draw solution, and to separate fresh water from the pre-treated sea water through member exchange with the draw solution; a recovery module configured to recover the draw solution and separate desalinated treatment water from the mixture solution; and a draw solution tank configured to store the draw solution recovered by the recovery module and to supply the draw solution to the forward osmosis membrane module; a product water tank on the ship configured to store the fresh water produced by the forward osmosis process unit; and a ballast water tank on the ship configured to store the ballast water produced by the forward osmosis process unit, wherein the ballast water produced by the forward osmosis process unit includes a portion of the draw solution of the mixture solution. 2. The ballast water treatment apparatus according to claim 1 , further comprising an economizer, wherein the recovery module recovers the draw solution using heat supplied from the economizer for absorbing waste heat of combustion gas discharged from an engine of a ship after combustion so as to supply the draw solution to the draw solution tank, and the separated fresh water is supplied to the product water tank. 3. The ballast water treatment apparatus according to claim 2 , wherein the recovery module comprises a carbon dioxide absorber which absorbs carbon dioxide of the combustion gas into the recovered draw solution so that the draw solution absorbing the carbon dioxide is recovered to the draw solution tank. 4. The ballast water treatment apparatus according to claim 1 , wherein the recovery module comprises: a carbon dioxide separator, wherein the carbon dioxide separator separates carbon dioxide by absorbing waste heat of combustion gas discharged from an engine of a ship after combustion, a liquid phase separator, wherein the liquid phase separator separates the draw solution using the separated carbon dioxide, and a separation membrane, wherein the separation membrane separates the fresh water from the liquid phase separator. 5. The ballast water treatment apparatus according to claim 4 , wherein the recovery module further comprises a carbon dioxide contactor which allows the draw solution separated from the liquid phase separator to come into contact with carbon dioxide of the combustion gas so that the draw solution coming into contact with the carbon dioxide is supplied to the draw solution tank. 6. The ballast water treatment apparatus according to claim 1 , wherein the recovery module comprises a separation membrane which separates the draw solution and the fresh water from the mixture solution using surplus power supplied from a ship. 7. The ballast water treatment apparatus according to claim 1 , wherein the recovery module comprises a magnetic separator which separates the draw solution and the fresh water from the mixture solution using surplus power supplied from a ship. 8. The ballast water treatment apparatus according to claim 1 , wherein the recovery module comprises: a cooler operated by surplus power supplied from a ship, a precipitation tank for precipitating the draw solution by lowering a temperature of the draw solution through the cooler and supplying the crystallized draw solution to the draw solution tank, and further comprises a separation membrane which separates the fresh water from the precipitation tank by the supplied surplus power. 9. The ballast water treatment apparatus according to claim 8 , further comprising an economizer, and wherein the recovery module further comprises a first heat exchanger which heats and dissolves the crystallized draw solution supplied to the draw solution tank using heat supplied from the economizer for absorbing waste heat of combustion gas discharged from an engine of the ship after combustion. 10. The ballast water treatment apparatus according to claim 9 , wherein the recovery module further comprises a second heat exchanger which heats the pre-treated sea water supplied to the forward osmosis membrane module using the heat supplied from the economizer. 11. The ballast water treatment apparatus according to claim 1 , further comprising a filter part for filtering the sea water collected through the water collection part, and a sea water pump for pumping the sea water such that the sea water is collected through the water collection part and supplying the sea water filtered by the filter part to the pre-treatment part. 12. The ballast water treatment apparatus according to claim 1 , wherein the draw solution is a material belonging to one of a volatile material group, an inorganic material group, an organic material group, and a synthesis material group.
Originating from marine vessels, ships and boats, e.g. bilge water or ballast water · CPC title
Reverse-osmosis · CPC title
Osmotic agents; Draw solutions · CPC title
Specific gas distributors or gas intakes · CPC title
Filtration · CPC title
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