AU549841B2

AU549841B2 – De-salinator for brackish -or salt-water
– Google Patents

AU549841B2 – De-salinator for brackish -or salt-water
– Google Patents
De-salinator for brackish -or salt-water

Info

Publication number
AU549841B2

AU549841B2
AU14762/83A
AU1476283A
AU549841B2
AU 549841 B2
AU549841 B2
AU 549841B2
AU 14762/83 A
AU14762/83 A
AU 14762/83A
AU 1476283 A
AU1476283 A
AU 1476283A
AU 549841 B2
AU549841 B2
AU 549841B2
Authority
AU
Australia
Prior art keywords
water
chamber
salinator
salt
brackish
Prior art date
1982-04-27
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)

Ceased

Application number
AU14762/83A
Other versions

AU1476283A
(en

Inventor
Ian Lloyd
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

Nautical Services Pty Ltd

Original Assignee
Nautical Services Pty Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
1982-04-27
Filing date
1983-04-27
Publication date
1986-02-13
Family has litigation

First worldwide family litigation filed
litigation
Critical
https://patents.darts-ip.com/?family=25615563&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=AU549841(B2)
“Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.

1983-04-27
Application filed by Nautical Services Pty Ltd
filed
Critical
Nautical Services Pty Ltd

1983-04-27
Priority to AU14762/83A
priority
Critical
patent/AU549841B2/en

1983-11-21
Publication of AU1476283A
publication
Critical
patent/AU1476283A/en

1986-02-13
Application granted
granted
Critical

1986-02-13
Publication of AU549841B2
publication
Critical
patent/AU549841B2/en

2003-04-27
Anticipated expiration
legal-status
Critical

Status
Ceased
legal-status
Critical
Current

Links

Espacenet

Global Dossier

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Classifications

Y—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

Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE

Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE

Y02A20/00—Water conservation; Efficient water supply; Efficient water use

Y02A20/124—Water desalination

Description

Title: “DE-SALINATOR FOR BRACKISH – OR SALT-WATER” BACKGROUND OF THE INVENTION
(1) Field of the Invention
This invention relates to a de-salinator for brackish – or salt-water which is particularly useful for, but not limited to, marine applications.
(2) Brief Description of the Prior Art
The marine de-salinators presently available have a number of problem areas. Firstly, they use electric pressure pumps to operate the eductors. These pumps require generators and/or alternators driven by the main and/or auxiliary engines of the watercraft for their power. As the engines must operate at, e.g. 3000 rpm to provide sufficient power, fuel is wasted when the engines are run at those speeds solely to generate electricity for the pumps. Secondly, the pumps drive the eductors under pressure and bypass valves must be provided in an attempt to maintain the pressures in the eductors at a substant- ially constant value, therefore maintaining the con¬ densation production rate at a constant. Thirdly, the “still”-type de-salinators require regular de¬ scaling and have a low output of fresh water while the osmosis-type require careful operation on start- up to prevent membrane damage.
BRIEF SUMMARY OF THE PRESENT INVENTION It is an object of the present invention to provide a de-salinator which avoids the need for generators and/or alternators to power the pumps. It is a preferred object to provide a de-sal¬ inator which can be operated over the full operating range of the engine(s).
It is a further preferred object to provide a de-salinator where the eductors are powered by suction pumps which prevent overloading of the eductors
OMPI S

It is a still further preferred object to provide a de-salinator which will operate at relative low heating temperatures.
It is a still further preferred object to provide a de-salinator where the de-salinator chamber is manufactured from fibreglass or other suitable plastics material.
Other preferred objects will become apparent from the following description. In one aspect, the invention resides in a de-salinator for brackish – or salt-water of the type including: a de-salinat±on chamber; a heat exchanger in the lower portion of the chamber to boil the brackish or salt-water; at least one condensor coil in the upper portion of the chamber to condense the de-salinated water vapour generated by the boiling water; at least one baffle between the heat exchanger and the condensor coils; and at least one outlet for the condensed de-salinated water from the chamber, wherein: the condensor coil or coils are cooled by the water drawn from the supply of the brackish – or salt-water by a suction pump, and the water from the condensor coil or coils is drawn through an eductor which is connected to the chamber to produce at least a partial vacuum in the chamber.
Preferably a second eductor, powered by a second suction pump, is provided to draw off the de¬ salinated water from the chamber. Preferably the suction pump draws fresh water from a fresh water tank, in which the de-salinated water is stored, to power the eductor. Preferably the first eductor also draws off
Oh___

coήcentrated brine from the bottom of the de-salination chamber.
Preferably the first eductor is also connected to the overflow outlet for the chamber to draw off any excess water in the chamber.
Preferably, when the engine driving the suction pumps is switched off, air is bled into the chamber to return it to atmospheric pressure.
Preferably the heat exchanger receives hot water from the engine driving the suction pumps, or from a solar heat water collector.
Preferably a portion of the brackish water or salt-water, after it has been heated in the condensor coils , is fed into the desalination chamber to maintain the water level in the chamber at a desired level.
BRIEF DESCRIPTION OF THE DRAWINGS To enable the invention to be fully understood, a preferred embodiment will now be described with reference to the accompanying drawings, in which: FIG. 1 is a perspective front view of the de-salination chamber and a schematic view of the associated circuit for a marine application;
FIG. 2 is a sectional end view of the chamber, taken on line 2-2 on FIG. 1; and FIG. 3 is a sectional side view of an eductor suitable for the invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT The de-salination chamber 10 has a substant¬ ially elliptical shell 11 closed at each end by removable end plates 12, the shell and end plates being formed from fibreglass. An 0-ring is provided in a groove around each end of the shell to seal the end plates to the shell and self-tapping fasteners secure the end plates to the shell. The bottom portion of the chamber provides

a container for the brackish – or salt-water 13 to be treated, the level of the water being limited by an overflow outlet 14.
Inclined baffles 15 lead up to a pair of spaced vertical baffles 16 with a central mesh screen 17 which prevents froth entering the condensation chamber 18 in the upper portion of the de-salinator.
At the top of the condensation chamber 18, the vapour is condensed on a pair of condensing tubes 19 provided sinuously along each side of the conden¬ sation chamber 18. The condensation runs down the sides of the shell 11 or the upper faces of the baffles 15 to condensate collection chambers 20, from which the condensate can be drawn off via condensate outlets 21.
A heat exchanger 22, comprising sinuous copper pipes, is provided in the bottom of the de-sal¬ inator 10 and is connected to a source of hot water by hot water pipes 23. A spray nozzle 24 is connected to the outlet side of the condensing tubes 19 via a valve 25 which enables a portion of the hot brackish – or salt-water to be sprayed into the de-salination chamber to maintain the volume of brackish – or salt-water 13 at a desired level. Concentrated brine is drawn off from the bottom of the de-salinator via a brine outlet 26.
The operation of the de-salinator will now be described.
Hot water, e.g. at a temperature of 32°C or greater, is pumped from the cooling system of the main engine 27 through the heat exchanger 22 via hot water pipes 23. At temperatures greater than 85°C, a thermo¬ statically controlled valve 28 bypasses a portion of the water through a marine heat exchanger 29 before returning the now-cooled water to the engine 27 to

to prevent overheating.
Salt-water is sucked from the sea through a sea cock 30 and filter 31 and passes through an in.let pipe 32 to a manifold 33 which distributes the incoming water to the condensing tubes 19. The now- heated salt-water enters an exhaust manifold 34 and flows through an outlet pipe 35 to an eductor 36 which has its outlet connected to an engine-driven suction pump 37. The outlet from the pump returns the heated salt-water to the sea. A portion of the hot salt water flows’ from the manifold 34 through the valve 25 to the spray nozzle 24 to maintain the level of the salt-water 13 at a predetermined level. A sight glass 38 in the shell (or in one of the end plates 12) enables the level to be checked.
The inlet of the eductor 36 is connected to the brine outlet 26 via a flow glass 39 and scavenge valve 40, to draw off any concentrated brine in the de-salinator, and to the overflow outlet 14 via a flow glass 41 and overflow valve 42. A balance distributor 43 and check valve 44 upstream of the inlet to the eductor 36 maintains the desired flow from the brine outlet 26 and overflow outlet 14 to the eductor 36. The vacuum generated by the eductor 36 reduces the pressure in the de-salinator to lower the boiling temperature for the salt-water 13. The reduced pressure in the de- salinator enables the water 13 to be boiled at a temperature of, for example 32°C.
Referring to FIG. 3, the eductor 36 has a main body with a central bore 36a having an initial construct¬ ion 36b. The line 44a connected to the check valve 44 enters the body at an angle and the construction 36c formed in the bore generates a vacuum due to the flow of water through the construction. A second engine driven suction pump 45, driven

off a common shaft with the suction pump 37, draws water through a second eductor 46 from the fresh water tank 47. The water line 48 interconnecting the water tank 47 to the eductor 46 is spaced above the bottom of the tank to ensure a reserve supply of water is contained in the tank 47. The inlet of the eductor 46 is connected to the condensate out¬ lets 21 via a fresh water line 49, fitted with a salinity monitor 50, and a manifold 51. A check valve 52 prevents the fresh water from the tank 47 being drawn into the desalinator when the pump 45 is switched off. Water from the tank 47 may be fed to a reservoir 47a which provides additional storage capacity. The heat exchanger 22 boils the salt-water
13 and vapour “rises up into the condensation chamber 18 where it condenses on the condensing tubes 19. The mesh screen 17 traps any froth in the vapour and prevents it from entering the condensation chamber. The fresh water drips and runs into the condensate collection chambers 20, while the concentrated brine which remains drips back into the lower portion of the desalinator and drawn off by the brine outlet 26.
The eductor 36, which produces the partial vacuum in the desalinator, also draws off any excess water 13 in the de-salinator via the overflow outlet 14.
Check valve 44 is provided intermediate the outlets 26, 14 and the eductor 36 and this may be controlled by a diaphragm valve on the output side of the pump 37. When the engine 30 is switched off, the pressure on the downstream of the pump 37 drops and the diaphragm valve closes the check valves 44 to prevent the brine and salt water being sucked back into the de¬ salinator. The check valve 44 may also include an air
Q-^-

bypass which operates to allow air into the de-salinator, and so destroy the vacuum in the de-salinator, when the valve is closed when the engine is switched off. This means that the de-salinator is evacuated each time the engine is operated and the de-salinator is returned to atmospheric pressure when the engine is switched off.
The de-salinator provides a simple and efficient means for de-salinating salt-water or brackish water and its efficiency as a heat exchanger means that the marine heat exchanger 29 is only necessary for large capacity engines.
Releasable connectors between the lines and the pipes on the de-salinator and the removable end plates 12 enable any repairs or maintenance to the de- salinator to be effected simply and quickly while the .elimination of the electric pumps removes a number of potential problem areas. A removable plug 53 in one of the end plates 12 enables acid to be placed in the de-salinator, when not in use, to descale the heat exchanger pipes 22.
Whilst a marine application has been specificall described, the unit may be used in, for example, desert areas to purify brackish water and the hot water for the heat exchanger 22 may be provided by solar hot water collectors while the pumps may be driven by a steam motor (the steam being generated in a solar collector) or by electric motors powered by solar electricity-generat¬ ing arrays or panels.
Various changes and modifications may be made to the embodiment described and illustrated without departing from the scope of the present invention.

Claims (7)

1. A de-salinator for brackish – or salt-water of the type including: a de-salination chamber; a heat exchanger in the power portion of the chamber to boil the brackish or salt-water; at least one condensor coil in the upper portion of the chamber to condense the de-salinated – water vapour generated by the boiling water; at least one baffle between the heat exchanger and the condensor coils; and at least one outlet for the condensed de¬ salinated water from the chamber, wherein: the condensor coil or coils are cooled by the water drawn from the supply of the brackish – or salt-water by a suction pump, and the water from the condensor coil or coils is drawn through an eductor which is connected to the chamber to produce at least a partial vacuum in the chamber.

2. A de-salinator as claimed in Claim 1 wherein.- a second eductor, powered by a second suction pump, is provided to draw off the de-salinated water from the chamber, the second suction pump drawing fresh water from a fresh water storage tank, in which the de-salinated water is stored, to power the second eductor.

3. A de-salinator as claimed in Claim 1 wherein: the first eductor is connected to a brine outlet at the bottom of the chamber to draw off concen¬ trated brine from the chamber and to an overflow outlet for the chamber to draw off any excess brackish – or salt-water in the chamber, the partial vacuum being formed by drawing air and/or vapour through the overflow outlet.

4. A de-salinator as claimed in Claim 1 or Claim 2
< - wherein: the heat exchanger receives hot water from the engine driving the suction pump or pumps. 5. A de-salinator as claimed in Claim 1 wherein: a portion of the brackish - or salt-water, after it has been heated in the condensor coil or coils, is fed to the chamber to maintain the water level in the chamber at a desired level. 6. A de-salinator as claimed in Claim 2 wherein: a pair of condensor coils are provided in the chamber above a respective condensate chamber along the junction of the baffles with the chamber walls, the inlet and outlets of the coils being connected to respective manifolds. 7. A de-salinator as claimed in Claim 1 wherein: the walls of the chamber are formed of heat insulating material to limit the loss of heat from the chamber. AU14762/83A 1982-04-27 1983-04-27 De-salinator for brackish -or salt-water Ceased AU549841B2 (en) Priority Applications (1) Application Number Priority Date Filing Date Title AU14762/83A AU549841B2 (en) 1982-04-27 1983-04-27 De-salinator for brackish -or salt-water Applications Claiming Priority (3) Application Number Priority Date Filing Date Title AUPF3754 1982-04-27 AUPF375482 1982-04-27 AU14762/83A AU549841B2 (en) 1982-04-27 1983-04-27 De-salinator for brackish -or salt-water Publications (2) Publication Number Publication Date AU1476283A AU1476283A (en) 1983-11-21 AU549841B2 true AU549841B2 (en) 1986-02-13 Family ID=25615563 Family Applications (1) Application Number Title Priority Date Filing Date AU14762/83A Ceased AU549841B2 (en) 1982-04-27 1983-04-27 De-salinator for brackish -or salt-water Country Status (1) Country Link AU (1) AU549841B2 (en) Cited By (1) * Cited by examiner, † Cited by third party Publication number Priority date Publication date Assignee Title AU639743B2 (en) * 1990-01-23 1993-08-05 Mikio Sakurai Irrigation system and irrigation method 1983 1983-04-27 AU AU14762/83A patent/AU549841B2/en not_active Ceased Cited By (1) * Cited by examiner, † Cited by third party Publication number Priority date Publication date Assignee Title AU639743B2 (en) * 1990-01-23 1993-08-05 Mikio Sakurai Irrigation system and irrigation method Also Published As Publication number Publication date AU1476283A (en) 1983-11-21 Similar Documents Publication Publication Date Title US4664751A (en) 1987-05-12 De-salinator for brackish salt water US4282070A (en) 1981-08-04 Energy conversion method with water recovery US4420373A (en) 1983-12-13 Energy conversion method and system CN108455692B (en) 2021-01-22 Multi-heat-source ship seawater desalination system AU2005284554A1 (en) 2006-03-23 Seawater desalination plant US3440147A (en) 1969-04-22 Combined heat load cooler and sea water desalination still BE1024466B1 (en) 2018-02-28 Mechanical water vapor desalination unit JP5672450B2 (en) 2015-02-18 Fresh water generator and fresh water generation method US3499827A (en) 1970-03-10 Distillation plant US3300392A (en) 1967-01-24 Vacuum distillation including predegasification of distilland RU2412909C1 (en) 2011-02-27 Desalination installation IL30935A (en) 1971-08-25 Condensing power plant system AU549841B2 (en) 1986-02-13 De-salinator for brackish -or salt-water CN1597540A (en) 2005-03-23 Sea water desalination method using air saturation humidity difference US11465068B2 (en) 2022-10-11 Multi-stage flash (MSF) reversal system and method FR2958179A1 (en) 2011-10-07 INSTALLATION OF SEA WATER DESALINATION BY MULTI-EFFECT DISTILLATION EP0044294A1 (en) 1982-01-27 A desalination apparatus with power generation WO2014003574A1 (en) 2014-01-03 Heat exchanger facility JPH0632802B2 (en) 1994-05-02 Demineralizer for salt water or salt water CN112624235A (en) 2021-04-09 Based on thermoelectric type economic benefits and social benefits condensation structure and sea water desalination device CN2641022Y (en) 2004-09-15 Seawater desalination appts. utilizing air saturation and wetness difference WO2002062708A1 (en) 2002-08-15 Method and device for production of distilled fluid and exergy Tleimat et al. 1982 Comparative productivity of distillation and reverse osmosis desalination using energy from solar ponds JP5979395B2 (en) 2016-08-24 Fresh water generator and fresh water generation method AU2021105568A4 (en) 2021-10-14 An apparatus for water distillation and method thereof
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