US20190091629A1 - Reverse osmosis water production apparatus - Google Patents
Reverse osmosis water production apparatus Download PDFInfo
- Publication number
- US20190091629A1 US20190091629A1 US16/129,783 US201816129783A US2019091629A1 US 20190091629 A1 US20190091629 A1 US 20190091629A1 US 201816129783 A US201816129783 A US 201816129783A US 2019091629 A1 US2019091629 A1 US 2019091629A1
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- US
- United States
- Prior art keywords
- reverse osmosis
- osmosis membrane
- water production
- production apparatus
- section
- Prior art date
- 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.)
- Abandoned
Links
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 138
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 65
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 32
- 239000012528 membrane Substances 0.000 claims abstract description 91
- 239000013535 sea water Substances 0.000 description 10
- 239000012267 brine Substances 0.000 description 7
- 230000002706 hydrostatic effect Effects 0.000 description 7
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 7
- 238000010612 desalination reaction Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000005086 pumping Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 238000009428 plumbing Methods 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000003190 augmentative effect Effects 0.000 description 1
- 230000003796 beauty Effects 0.000 description 1
- 235000012206 bottled water Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 238000011176 pooling Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 230000035899 viability Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
Classifications
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- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/08—Apparatus therefor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/025—Reverse osmosis; Hyperfiltration
- B01D61/026—Reverse osmosis; Hyperfiltration comprising multiple reverse osmosis steps
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- B63B2043/047—Improving safety of vessels, e.g. damage control, not otherwise provided for reducing risk of capsizing or sinking by improving stability by means of hull shapes comprising a wide hull portion near the design water line, and a slender, buoyancy providing, main hull portion extending towards the bottom
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- B63B39/02—Equipment to decrease pitch, roll, or like unwanted vessel movements; Apparatus for indicating vessel attitude to decrease vessel movements by displacement of masses
- B63B39/03—Equipment to decrease pitch, roll, or like unwanted vessel movements; Apparatus for indicating vessel attitude to decrease vessel movements by displacement of masses by transferring liquids
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- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- 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
- Y02A20/131—Reverse-osmosis
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- 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
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- 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
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- Y02W10/00—Technologies for wastewater treatment
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- Y02W10/33—Wastewater or sewage treatment systems using renewable energies using wind energy
Definitions
- RO systems for high volume seawater to fresh water production are generally land based and are typically either in the form of large central plants near the coast, or smaller systems, some packaged in a shipping container type enclosure.
- Regions experiencing significant drought (or other interruption to the regular water supply) require the prompt establishment of a substantial new water supply.
- Large central RO plants may require years of planning and permitting, along with the need for a substantial electric power supply.
- high capacity pipelines are required to draw seawater in to the system and to discharge brine back to the ocean. The pooling of brine around the end of the brine discharge pipe can have adverse impacts on marine life in the vicinity and is a key hurdle in environmental permitting.
- Marine barge mounted systems are becoming available, which can transit at sea, stationing in coastal areas in need of freshwater. Some of these have an on-board electric power generating systems and fuel supplies while others rely on power from shore.
- RO systems are designed to meet the on-board water requirements.
- Most desalination systems on marine vessels are based on RO membranes contained in tubular pressure vessels which are orientated horizontally to fit a horizontal spatial arrangement in the vessel.
- An RO surface vessel may impose an undesirable view on coastline natural beauty, which can be particularly undesirable if the vessel is moored in an area which is dependent on tourism.
- a permanently moored RO surface vessel for long-term commercial water delivery to shore is not easily moved out of harm's way.
- Marine surface vessels are also subject to extreme environmental forces of wind and waves, where pitch and roll in high seas can test survival. Vessels with a large surface profile are especially vulnerable to high winds.
- a reverse osmosis water production apparatus for use in a body of water comprising;
- the first section is substantially cylindrical.
- the second section is substantially cylindrical.
- a diameter of the first section is greater than a diameter of the second section, more preferably around two times the diameter of the second section.
- the reverse osmosis membrane tubes are arranged in a substantially concentric ring around the passage.
- the reverse osmosis membrane tubes are arranged to form an inner concentric ring and an outer concentric ring around the passage.
- a reverse osmosis membrane tube from the inner ring and a reverse osmosis tube from the outer ring are connected together to form a first reverse osmosis membrane tube module.
- a reverse osmosis membrane tube from the inner ring and two adjacent reverse osmosis tubes from the outer ring are connected together to form a second reverse osmosis membrane tube module.
- the apparatus comprises a plurality of first reverse osmosis membrane tube modules and a plurality of second reverse osmosis membrane tube modules.
- first and second reverse osmosis membrane tube modules are arranged alternately.
- a spacing between the first and second reverse osmosis membrane tube modules is such that one of the first reverse osmosis membrane tube modules must be removed before any one of the second reverse osmosis membrane tube modules can be removed.
- the passage is selectively communicable with the first section.
- the passage extends through the first section of the buoy.
- the apparatus comprises moving means capable of moving at least one reverse osmosis membrane tube into the passage.
- the moving means is capable of moving an entire first reverse osmosis membrane tube module into the passage.
- the moving means is capable of moving an entire second reverse osmosis membrane tube module into the passage.
- the moving means comprises an arm.
- the arm is rotatably connected a support member.
- the base is rotatably connected to the second section.
- connection between the base and the arm is offset from a centre of the chamber.
- an upper surface of the buoy comprises a deck, wherein the deck is provided with an access way which is substantially aligned with the elongate chamber.
- the buoy comprises a lifting means for lifting at least one reverse osmosis membrane tube up to the deck.
- the lifting means comprises a crane.
- the apparatus comprises one or more additional sections, each additional section configured to define an additional elongate chamber which extends downward beneath the water in use, the additional elongate chamber provided with a plurality of additional elongate reverse osmosis membrane tubes, wherein a longitudinal axis of each additional reverse osmosis membrane tube is substantially parallel with a longitudinal axis of the additional elongate chamber;
- the apparatus comprises a ballast tank at a distal end of the apparatus to the first section.
- FIG. 1 Is a side view of an embodiment of a reverse osmosis water production apparatus of the present invention
- FIG. 2 is a side view of the apparatus of FIG. 1 with an outer wall of the apparatus not shown to reveal the internal RO tube arrangement of the apparatus;
- FIG. 3 is a top view of the second section of the apparatus of FIG. 1 ;
- FIG. 4 is a perspective view of the bulkheads and moving means of the second section
- FIG. 5 is a top view of the second section of the apparatus of FIG. 1 showing the moving means engaged with a first reverse osmosis membrane tube module;
- FIG. 6 is a perspective view of the moving means connected to a first reverse osmosis membrane tube module, with the remainder of the modules and the outer wall of the second section not shown for clarity.
- a reverse osmosis (RO) water production apparatus is generally referenced by arrow 100 .
- the apparatus 100 is configured as a submersible spar buoy and is intended for use as a desalination apparatus.
- the apparatus 100 is configured to float in a body of water, in particular saline water, and comprises a first section 1 which defines a buoyancy chamber and an elongate second section 2 in operation, which extends downward beneath the waterline W when in RO operation.
- both the first and the second sections 1 , 2 are substantially cylindrical.
- the diameter of the first section 1 is preferably greater than the diameter of the second section 2 (for example around twice the diameter of the second section) so that in operation, when all the RO membrane tubes and plumbing are filled with water, the centre of buoyancy CB of the apparatus 100 is higher than the centre of mass CM and sufficiently separated to provide vertical stability.
- the second section 2 defines an elongate chamber 3 which is provided with a plurality of elongate reverse osmosis membrane tubes 4 .
- Each tube contains reverse osmosis membranes (not shown).
- the RO tubes 4 are arranged around a passage 5 which is preferably substantially central to the chamber.
- the tubes 4 function as RO pressure vessels for the pumped and pressurized seawater and are provided with valving at suitable inlets for raw water and outlets for product (desalinated) water and brine waste water.
- a longitudinal axis L 1 of each tube 4 is preferably substantially parallel with a longitudinal axis L 2 of the second section 2 .
- the longitudinal axes of the second section 2 and the tubes 4 are preferably orientated substantially vertically in use.
- the first section may have a diameter of around 8.2 m and the second section may have a diameter of around 3.5 m and a length of around 8.5 m.
- the passage may have a diameter of around 1.5 m.
- the reverse osmosis membrane tubes 4 are arranged to form at least one ring around the passage 5 .
- the tubes form an inner ring 6 and a concentric outer ring 7 .
- a reverse osmosis membrane tube 4 a from the inner ring 6 is connected to a reverse osmosis membrane tube 4 b from the outer ring 7 by suitable bracketry 8 (an example of which is shown in FIG. 6 ) to form a first reverse osmosis membrane tube module 10 .
- a second reverse osmosis membrane tube 4 c from the inner ring 6 is connected to two further reverse osmosis membrane tubes 4 d from the outer ring 7 by suitably bracketry to form a second reverse osmosis membrane tube module 11 .
- the inner and outer rings 6 , 7 are formed by alternating first and second reverse osmosis membrane tubes modules 10 , 11 .
- arranging alternating first and second reverse osmosis membrane tubes modules 10 , 11 in this way creates a very compact arrangement of alternating first and second reverse osmosis membrane tubes 4 is created which allows for tube module removal.
- Other combinations of tubes and modules may be arranged to provide maximum compactness with full accessibility.
- an upper surface 12 ( FIG. 1 ) of the apparatus 100 is provided with an access way 13 , for example a hatch, which is substantially aligned with the passage 5 in the second section 2 .
- the portion of the first section 1 between the access way 13 and the passage 5 preferably also comprises a clear passage 14 , or can at least be configured to provide a passage 14 (for example by opening of a hatch between the first and second sections and/or moving of equipment in the first section 1 ).
- a lifting means typically a crane (not shown), provided on an exterior of the first section 1 can be used to lift one or more reverse osmosis membrane tubes 4 from the second section 2 to the exterior of the first section 1 , from where the tube 4 can be removed for servicing, repair or replacement.
- the second section 2 may be provided with a moving means 20 ( FIG. 4 ) which is capable of moving a reverse osmosis membrane tube 4 , or a reverse osmosis membrane tube module 10 , 11 , from its normal operating position to a position in the passage 5 from which it can be conveniently serviced and/or lifted by the lifting means.
- FIGS. 4 to 6 show one embodiment of such a moving means 20 which is adapted for use with first and second reverse osmosis membrane tube modules 10 , 11 .
- a preferred embodiment of the moving means 20 comprises a support member 21 which extends between an upper bulkhead 22 and a lower bulkhead 23 .
- the support member 21 is connected to the bulkheads 22 , 23 by rotatable connections 24 , 25 which allow the support member 21 to rotate around an annular path around the outside of the passage 5 , and to rotate about a rotational axis which intersects the connections 24 , 25 .
- the moving means 20 comprises at least one, and preferably a plurality of arms 26 .
- Each arm 26 is connected to the support member 21 by a respective rotatable connection 27 .
- a distal end of each arm 26 is provided with engagement means 28 for engaging a reverse osmosis membrane tube 4 and/or a reverse osmosis membrane tube module 10 , 11 .
- the engagement means 28 comprises a pin 29 which is adapted to engage an aperture 30 in a bracket 8 which is attached to the reverse osmosis membrane tube 4 or reverse osmosis membrane tube module 10 , 11 , but other engagement means (for example gripping means) may be provided.
- valves in the sea water intake manifold, the brine discharge outlet, and the product water feed line Prior to RO module removal, valves in the sea water intake manifold, the brine discharge outlet, and the product water feed line are all closed, isolating and disconnecting the module for removal of the module while the other modules continue to function.
- each arm 26 is engaged with the reverse osmosis membrane tube 4 or module 10 , 11 by moving the pin 29 underneath the aperture 30 and then moving the arm 26 upward by means of a suitable actuator (not shown) until the arm 26 is bearing the weight of the reverse osmosis membrane tube 4 or module 10 , 11 .
- the tube/module can then be disconnected from the second section 2 and moved into the passage 5 by articulation of the arm 26 and support member 21 . Once in the passage 5 , maintenance tasks can be performed on the tube or module and/or the tube or module can be lifted out of the apparatus 100 or reinstalled in its operating position.
- a ladder 31 is provided between the bulkheads 22 , 23 at an outer periphery of the passage 5 , and may be connected to the support member 21 so as to rotate with the support member.
- the ladder 31 may be used to reach the lower bulkhead 23 as well as for access to the tube/module mounting components and pipework.
- the spacing between the first and second reverse osmosis membrane tube modules 10 , 11 is relatively small in order to make the second section 2 as small in diameter as possible.
- the reverse osmosis membrane tube modules 10 , 11 are sufficiently closely spaced that it is not possible to move any of the second reverse osmosis membrane tube modules 11 into the passage 5 without first removing an adjacent reverse osmosis membrane tube module 10 .
- Compact spacing of the membrane tube modules 10 , 11 is advantageous for a number of reasons, including reducing the diameter of the second section, thereby reducing the cross-sectional area which is acted on by wave and current action, as well as mass buoyancy balance and control, as is described further below.
- the apparatus 100 may comprise one or more additional sections 2 a connected below the second section 2 , each additional section 2 a having the same features as the second section 2 .
- a watertight hatch (not shown) is preferably provided at each bulkhead.
- Each additional section 2 a is preferably close to neutrally buoyant (when the reverse osmosis membrane tubes and associated pipework are filled with water) so that connection of additional sections 2 a does not move the centre of mass too close to the centre of buoyancy, which would compromise the vertical stability of the apparatus.
- the apparatus 100 comprises a ballast tank 32 at the lower end of the apparatus (distal the first section 1 ). The ballast tank 32 water volume can be adjusted as required to make small buoyancy adjustments relative to the centre of mass of the apparatus 100 .
- the apparatus may need to traverse shallow water during departure from ports and in coastal transit.
- the apparatus 100 may be deployed horizontally, floating on the ocean surface, and may be towed by a service vessel to its operating site. At the site, while the apparatus 100 is still in a horizontal position, dry connections can be made for the mooring lines to the seabed anchors and the water conduit pipe and power cable to shore (or other power source).
- the RO system is activated with its on-board seawater pumps filling the membrane tubes 4 (and optionally the ballast tank 32 ), causing the mass of the lower end of the apparatus 100 to increase, whereby the apparatus gradually rotates 90 degrees to a vertical position.
- the membrane tubes 4 and any ballast tanks 32 can be pumped dry, reducing the mass at the lower end of the apparatus such that the reduced mass and added buoyancy gradually rotate the apparatus to a horizontal position for towing.
- the first section 1 When in the in-use or vertical orientation, the first section 1 penetrates the ocean surface with a low profile, while the second and additional sections 2 , 2 a may reach tens or hundreds of meters into deeper water.
- the freeboard above the water surface can be adjusted by ballast tank water volume adjustments.
- the apparatus 100 In operation the apparatus 100 is highly stable, with minimal surface exposure and response to wind loads, wave heave and wave orbital forces.
- the freeboard of the apparatus 100 is preferably sufficient to allow easy entry by crew for servicing via the topside access way/hatch 13 , while still presenting a very low surface profile which has minimal aesthetic impact.
- the apparatus may be required to completely submerge the apparatus, which can be effected by reducing positive vessel buoyancy to minimum, and by adapting the vertical mooring line to function as a tension leg system, whereby a winch can be activated to draw down the apparatus below the ocean surface.
- the preferred cylindrical shape of the sections making up the apparatus 100 is ideal to withstand increased hydrostatic pressure as the apparatus extends into deeper water.
- the second and additional sections contain the pumps, valves, actuators and controls to operate that section as a discrete unit.
- Each section 2 , 2 a may draw inlet seawater to a common manifold (for the section) as well as collecting product water and brine, each to respective outlet manifolds.
- Utilizing the hydrostatic pressure reduces the power needed to create a suitable pressure for reverse osmosis brine separation. At some depths the hydrostatic pressure may be sufficient that no additional pumping is required to drive the reverse osmosis process. The residual pressure of the product water reduces the power needed to lift the product water for delivery to shore.
- each second and additional section 2 , 2 a has a through-hull seawater inlet for the RO systems to utilize the exterior hydrostatic pressure differential compared to the surface atmospheric pressure to reduce the power needed to pump inlet seawater to the pressure required for efficient desalination by the RO membrane. This is accomplished when the product water line is vented to the ocean surface atmospheric pressure.
- the residual hydrostatic pressure of the product water after completing the reverse osmosis processes through the RO membranes reduces pumping power needed to lift the water to the surface.
- Using the hydrostatic pressure of the seawater at depth thus, enables reduced pumping pressure for the RO processes and for lifting the product to the surface resulting in lower cost for power.
- the apparatus 100 may be moored by a tension leg mooring to an anchor on the seabed. Additionally or alternatively the ballast tank 32 may be emptied to provide sufficient buoyancy to offset the flooded chamber.
- the apparatus 100 of the present invention may be powered by an on-shore power source or a separate on-water source.
- the apparatus 100 is particularly suited to make use of off-shore renewable energy sources such as wave energy power generators, current turbines and/or offshore wind turbines.
- the invention may also be said broadly to consist in the parts, elements and features referred to or indicated in the specification of the application, individually or collectively, in any or all combinations of two or more of said parts, elements or features.
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Abstract
Description
- This application claims priority of Australian Patent application serial no. 735748 filed on 22 Sep. 2017, the disclosure of which is incorporated herein by reference.
- The present invention relates to a reverse osmosis water production apparatus, and in particular, but not exclusively, to a desalination apparatus for use in a body of water.
- Reverse Osmosis (RO) systems for high volume seawater to fresh water production are generally land based and are typically either in the form of large central plants near the coast, or smaller systems, some packaged in a shipping container type enclosure.
- Regions experiencing significant drought (or other interruption to the regular water supply) require the prompt establishment of a substantial new water supply. Large central RO plants may require years of planning and permitting, along with the need for a substantial electric power supply. Furthermore, high capacity pipelines are required to draw seawater in to the system and to discharge brine back to the ocean. The pooling of brine around the end of the brine discharge pipe can have adverse impacts on marine life in the vicinity and is a key hurdle in environmental permitting.
- Marine barge mounted systems are becoming available, which can transit at sea, stationing in coastal areas in need of freshwater. Some of these have an on-board electric power generating systems and fuel supplies while others rely on power from shore.
- Most marine vessel's RO systems are designed to meet the on-board water requirements. Most desalination systems on marine vessels are based on RO membranes contained in tubular pressure vessels which are orientated horizontally to fit a horizontal spatial arrangement in the vessel.
- An RO surface vessel may impose an undesirable view on coastline natural beauty, which can be particularly undesirable if the vessel is moored in an area which is dependent on tourism.
- A permanently moored RO surface vessel for long-term commercial water delivery to shore is not easily moved out of harm's way. Marine surface vessels are also subject to extreme environmental forces of wind and waves, where pitch and roll in high seas can test survival. Vessels with a large surface profile are especially vulnerable to high winds.
- All references, including any patents or patent applications cited in this specification are hereby incorporated by reference. No admission is made that any reference constitutes prior art. The discussion of the references states what their authors assert, and the applicants reserve the right to challenge the accuracy and pertinency of the cited documents. It will be clearly understood that, although a number of prior art publications are referred to herein, this reference does not constitute an admission that any of these documents form part of the common general knowledge in the art, in New Zealand or in any other country.
- Unless the context clearly requires otherwise, throughout the description and the claims, the words “comprise”, “comprising”, and the like, are to be construed in an inclusive sense as opposed to an exclusive or exhaustive sense, that is to say, in the sense of “including, but not limited to”.
- It is an object of the present invention to address the foregoing problems or at least to provide the public with a useful choice.
- Further aspects and advantages of the present invention will become apparent from the ensuing description which is given by way of example only.
- According to one aspect of the present invention there is provided a reverse osmosis water production apparatus for use in a body of water comprising;
-
- a first section defining a buoyancy chamber;
- an elongate second section connected to the first section and configured to define an elongate chamber which extends downward beneath a waterline in use, the elongate chamber provided with a plurality of elongate reverse osmosis membrane tubes, each tube containing a reverse osmosis membrane, wherein a longitudinal axis of each reverse osmosis membrane tube is substantially parallel with a longitudinal axis of the elongate chamber;
- wherein the reverse osmosis membrane tubes are arranged around a passage.
- Preferably the first section is substantially cylindrical.
- Preferably the second section is substantially cylindrical.
- Preferably a diameter of the first section is greater than a diameter of the second section, more preferably around two times the diameter of the second section.
- Preferably the reverse osmosis membrane tubes are arranged in a substantially concentric ring around the passage.
- Preferably the reverse osmosis membrane tubes are arranged to form an inner concentric ring and an outer concentric ring around the passage.
- Preferably a reverse osmosis membrane tube from the inner ring and a reverse osmosis tube from the outer ring are connected together to form a first reverse osmosis membrane tube module.
- Preferably a reverse osmosis membrane tube from the inner ring and two adjacent reverse osmosis tubes from the outer ring are connected together to form a second reverse osmosis membrane tube module.
- Preferably the apparatus comprises a plurality of first reverse osmosis membrane tube modules and a plurality of second reverse osmosis membrane tube modules.
- Preferably the first and second reverse osmosis membrane tube modules are arranged alternately.
- Preferably a spacing between the first and second reverse osmosis membrane tube modules is such that one of the first reverse osmosis membrane tube modules must be removed before any one of the second reverse osmosis membrane tube modules can be removed.
- Preferably the passage is selectively communicable with the first section.
- Preferably the passage extends through the first section of the buoy.
- Preferably the apparatus comprises moving means capable of moving at least one reverse osmosis membrane tube into the passage.
- Preferably the moving means is capable of moving an entire first reverse osmosis membrane tube module into the passage.
- Preferably the moving means is capable of moving an entire second reverse osmosis membrane tube module into the passage.
- Preferably the moving means comprises an arm.
- Preferably the arm is rotatably connected a support member.
- Preferably the base is rotatably connected to the second section.
- Preferably the connection between the base and the arm is offset from a centre of the chamber.
- Preferably an upper surface of the buoy comprises a deck, wherein the deck is provided with an access way which is substantially aligned with the elongate chamber.
- Preferably the buoy comprises a lifting means for lifting at least one reverse osmosis membrane tube up to the deck.
- Preferably the lifting means comprises a crane.
- Preferably the apparatus comprises one or more additional sections, each additional section configured to define an additional elongate chamber which extends downward beneath the water in use, the additional elongate chamber provided with a plurality of additional elongate reverse osmosis membrane tubes, wherein a longitudinal axis of each additional reverse osmosis membrane tube is substantially parallel with a longitudinal axis of the additional elongate chamber;
-
- wherein the additional reverse osmosis membrane tubes are arranged around the additional passage.
- Preferably the apparatus comprises a ballast tank at a distal end of the apparatus to the first section.
- Further aspects of the present invention will become apparent from the following description which is given by way of example only and with reference to the accompanying drawings in which:
-
FIG. 1 Is a side view of an embodiment of a reverse osmosis water production apparatus of the present invention; -
FIG. 2 is a side view of the apparatus ofFIG. 1 with an outer wall of the apparatus not shown to reveal the internal RO tube arrangement of the apparatus; -
FIG. 3 is a top view of the second section of the apparatus ofFIG. 1 ; -
FIG. 4 is a perspective view of the bulkheads and moving means of the second section; -
FIG. 5 is a top view of the second section of the apparatus ofFIG. 1 showing the moving means engaged with a first reverse osmosis membrane tube module; and -
FIG. 6 is a perspective view of the moving means connected to a first reverse osmosis membrane tube module, with the remainder of the modules and the outer wall of the second section not shown for clarity. - Referring first to
FIGS. 1 and 2 , a reverse osmosis (RO) water production apparatus is generally referenced byarrow 100. In the embodiment shown in the figures theapparatus 100 is configured as a submersible spar buoy and is intended for use as a desalination apparatus. - The
apparatus 100 is configured to float in a body of water, in particular saline water, and comprises afirst section 1 which defines a buoyancy chamber and an elongatesecond section 2 in operation, which extends downward beneath the waterline W when in RO operation. In preferred embodiments both the first and thesecond sections first section 1 is preferably greater than the diameter of the second section 2 (for example around twice the diameter of the second section) so that in operation, when all the RO membrane tubes and plumbing are filled with water, the centre of buoyancy CB of theapparatus 100 is higher than the centre of mass CM and sufficiently separated to provide vertical stability. When the RO membrane tubes and plumbing is emptied of water vessel mass is reduced and buoyancy increased, and the CB moves in near proximity to the CM causing the vessel to rotate to a horizontal position on the ocean surface. - As seen in
FIGS. 2 and 3 , thesecond section 2 defines anelongate chamber 3 which is provided with a plurality of elongate reverseosmosis membrane tubes 4. Each tube contains reverse osmosis membranes (not shown). TheRO tubes 4 are arranged around apassage 5 which is preferably substantially central to the chamber. Thetubes 4 function as RO pressure vessels for the pumped and pressurized seawater and are provided with valving at suitable inlets for raw water and outlets for product (desalinated) water and brine waste water. A longitudinal axis L1 of eachtube 4 is preferably substantially parallel with a longitudinal axis L2 of thesecond section 2. The longitudinal axes of thesecond section 2 and thetubes 4 are preferably orientated substantially vertically in use. - In one non-limiting embodiment, the first section may have a diameter of around 8.2 m and the second section may have a diameter of around 3.5 m and a length of around 8.5 m. The passage may have a diameter of around 1.5 m.
- In preferred embodiments, the reverse
osmosis membrane tubes 4 are arranged to form at least one ring around thepassage 5. In the embodiment shown the tubes form aninner ring 6 and a concentricouter ring 7. - As can be seen in
FIG. 3 , in some embodiments a reverseosmosis membrane tube 4 a from theinner ring 6 is connected to a reverseosmosis membrane tube 4 b from theouter ring 7 by suitable bracketry 8 (an example of which is shown inFIG. 6 ) to form a first reverse osmosismembrane tube module 10. A second reverseosmosis membrane tube 4 c from theinner ring 6 is connected to two further reverseosmosis membrane tubes 4 d from theouter ring 7 by suitably bracketry to form a second reverse osmosismembrane tube module 11. In the embodiment shown the inner andouter rings membrane tubes modules FIG. 3 , arranging alternating first and second reverse osmosismembrane tubes modules osmosis membrane tubes 4 is created which allows for tube module removal. Other combinations of tubes and modules may be arranged to provide maximum compactness with full accessibility. - Over time, the reverse osmosis membranes drop in osmotic efficiency due to membranes clogging-up with particulates and scaling with mineral deposits. This leads to a requirement for membrane cleaning or replacement.
- Removal of one or more reverse
osmosis membrane tubes 4 is facilitated by thepassage 5. In preferred embodiments an upper surface 12 (FIG. 1 ) of theapparatus 100 is provided with anaccess way 13, for example a hatch, which is substantially aligned with thepassage 5 in thesecond section 2. The portion of thefirst section 1 between theaccess way 13 and thepassage 5 preferably also comprises aclear passage 14, or can at least be configured to provide a passage 14 (for example by opening of a hatch between the first and second sections and/or moving of equipment in the first section 1). In this way a lifting means, typically a crane (not shown), provided on an exterior of thefirst section 1 can be used to lift one or more reverseosmosis membrane tubes 4 from thesecond section 2 to the exterior of thefirst section 1, from where thetube 4 can be removed for servicing, repair or replacement. - In preferred embodiments the
second section 2 may be provided with a moving means 20 (FIG. 4 ) which is capable of moving a reverseosmosis membrane tube 4, or a reverse osmosismembrane tube module passage 5 from which it can be conveniently serviced and/or lifted by the lifting means.FIGS. 4 to 6 show one embodiment of such a moving means 20 which is adapted for use with first and second reverse osmosismembrane tube modules - Referring to
FIG. 4 in particular, a preferred embodiment of the movingmeans 20 comprises asupport member 21 which extends between an upper bulkhead 22 and alower bulkhead 23. Thesupport member 21 is connected to thebulkheads 22, 23 byrotatable connections support member 21 to rotate around an annular path around the outside of thepassage 5, and to rotate about a rotational axis which intersects theconnections - The moving means 20 comprises at least one, and preferably a plurality of
arms 26. Eacharm 26 is connected to thesupport member 21 by arespective rotatable connection 27. A distal end of eacharm 26 is provided with engagement means 28 for engaging a reverseosmosis membrane tube 4 and/or a reverse osmosismembrane tube module pin 29 which is adapted to engage anaperture 30 in abracket 8 which is attached to the reverseosmosis membrane tube 4 or reverse osmosismembrane tube module - Prior to RO module removal, valves in the sea water intake manifold, the brine discharge outlet, and the product water feed line are all closed, isolating and disconnecting the module for removal of the module while the other modules continue to function.
- In use, each
arm 26 is engaged with the reverseosmosis membrane tube 4 ormodule pin 29 underneath theaperture 30 and then moving thearm 26 upward by means of a suitable actuator (not shown) until thearm 26 is bearing the weight of the reverseosmosis membrane tube 4 ormodule second section 2 and moved into thepassage 5 by articulation of thearm 26 andsupport member 21. Once in thepassage 5, maintenance tasks can be performed on the tube or module and/or the tube or module can be lifted out of theapparatus 100 or reinstalled in its operating position. In preferred embodiments aladder 31 is provided between thebulkheads 22, 23 at an outer periphery of thepassage 5, and may be connected to thesupport member 21 so as to rotate with the support member. Theladder 31 may be used to reach thelower bulkhead 23 as well as for access to the tube/module mounting components and pipework. - As best seen in
FIG. 3 , in preferred embodiments the spacing between the first and second reverse osmosismembrane tube modules second section 2 as small in diameter as possible. In preferred embodiments the reverse osmosismembrane tube modules membrane tube modules 11 into thepassage 5 without first removing an adjacent reverse osmosismembrane tube module 10. Compact spacing of themembrane tube modules - In some embodiments the
apparatus 100 may comprise one or moreadditional sections 2 a connected below thesecond section 2, eachadditional section 2 a having the same features as thesecond section 2. A watertight hatch (not shown) is preferably provided at each bulkhead. By use of this modular configuration the potable water production water capacity of theapparatus 100 can be configured to match product water supply requirements. Eachadditional section 2 a is preferably close to neutrally buoyant (when the reverse osmosis membrane tubes and associated pipework are filled with water) so that connection ofadditional sections 2 a does not move the centre of mass too close to the centre of buoyancy, which would compromise the vertical stability of the apparatus. However, in preferred embodiments theapparatus 100 comprises aballast tank 32 at the lower end of the apparatus (distal the first section 1). Theballast tank 32 water volume can be adjusted as required to make small buoyancy adjustments relative to the centre of mass of theapparatus 100. - Deployment
- Rapid, low cost transit/transport is key to the economic viability of marine reverse osmosis (RO) systems and essential for emergency deployment for water supply. The apparatus may need to traverse shallow water during departure from ports and in coastal transit. In preferred embodiments the
apparatus 100 may be deployed horizontally, floating on the ocean surface, and may be towed by a service vessel to its operating site. At the site, while theapparatus 100 is still in a horizontal position, dry connections can be made for the mooring lines to the seabed anchors and the water conduit pipe and power cable to shore (or other power source). Once theapparatus 100 is secured, the RO system is activated with its on-board seawater pumps filling the membrane tubes 4 (and optionally the ballast tank 32), causing the mass of the lower end of theapparatus 100 to increase, whereby the apparatus gradually rotates 90 degrees to a vertical position. To remove theapparatus 100 back to a shore base, themembrane tubes 4 and anyballast tanks 32 can be pumped dry, reducing the mass at the lower end of the apparatus such that the reduced mass and added buoyancy gradually rotate the apparatus to a horizontal position for towing. - When in the in-use or vertical orientation, the
first section 1 penetrates the ocean surface with a low profile, while the second andadditional sections apparatus 100 is highly stable, with minimal surface exposure and response to wind loads, wave heave and wave orbital forces. The freeboard of theapparatus 100 is preferably sufficient to allow easy entry by crew for servicing via the topside access way/hatch 13, while still presenting a very low surface profile which has minimal aesthetic impact. In certain instances, it may be required to completely submerge the apparatus, which can be effected by reducing positive vessel buoyancy to minimum, and by adapting the vertical mooring line to function as a tension leg system, whereby a winch can be activated to draw down the apparatus below the ocean surface. - Depth Pressure Augmented Reverse Osmosis
- The preferred cylindrical shape of the sections making up the
apparatus 100 is ideal to withstand increased hydrostatic pressure as the apparatus extends into deeper water. - In a preferred embodiment the second and additional sections contain the pumps, valves, actuators and controls to operate that section as a discrete unit. Each
section - Utilizing the hydrostatic pressure reduces the power needed to create a suitable pressure for reverse osmosis brine separation. At some depths the hydrostatic pressure may be sufficient that no additional pumping is required to drive the reverse osmosis process. The residual pressure of the product water reduces the power needed to lift the product water for delivery to shore.
- In preferred embodiments, utilizing the exterior seawater hydrostatic pressure each second and
additional section - Safety Margin on Buoyancy
- Bulkheads and hatches isolate the second and
additional sections sections - In some embodiments (not shown) there may be excess buoyancy in the entire apparatus and the
apparatus 100 may be moored by a tension leg mooring to an anchor on the seabed. Additionally or alternatively theballast tank 32 may be emptied to provide sufficient buoyancy to offset the flooded chamber. - Power Source
- The
apparatus 100 of the present invention may be powered by an on-shore power source or a separate on-water source. However, theapparatus 100 is particularly suited to make use of off-shore renewable energy sources such as wave energy power generators, current turbines and/or offshore wind turbines. - The invention may also be said broadly to consist in the parts, elements and features referred to or indicated in the specification of the application, individually or collectively, in any or all combinations of two or more of said parts, elements or features.
- Where in the foregoing description reference has been made to integers or components having known equivalents thereof, those integers are herein incorporated as if individually set forth.
- It should be noted that various changes and modifications to the presently preferred embodiments described herein will be apparent to those skilled in the art. Such changes and modifications may be made without departing from the spirit and scope of the invention and without diminishing its attendant advantages. It is therefore intended that such changes and modifications be included within the present invention.
Claims (24)
Priority Applications (5)
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US17/087,309 US12102964B2 (en) | 2017-09-22 | 2020-11-02 | Reverse osmosis water production apparatus |
US17/163,295 US11660572B2 (en) | 2017-09-22 | 2021-01-29 | Wind and wave desalination vessel |
US17/391,884 US20210362094A1 (en) | 2017-09-22 | 2021-08-02 | Wind-Powered Direct Air Carbon Dioxide Capture for Ocean Sequestration |
US17/665,459 US20220274063A1 (en) | 2017-09-22 | 2022-02-04 | Wind-Powered Direct Air Carbon Dioxide Capture Device for Ocean Sequestration |
US17/726,434 US11701616B2 (en) | 2017-09-22 | 2022-04-21 | Sorbent emitter for direct air capture of carbon dioxide |
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WO2021087473A1 (en) | 2019-11-01 | 2021-05-06 | Natural Ocean Well Co. | Adhesively-bonded water separation cartridge module |
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JP2022549020A (en) * | 2019-11-01 | 2022-11-22 | ナチュラル オーシャン ウェル カンパニー | Submersible water desalination system with replaceable and dockable membrane modules |
US11529586B2 (en) * | 2019-11-01 | 2022-12-20 | Natural Ocean Well Co. | Adhesively-bonded water separation cartridge module |
JP7270872B2 (en) | 2019-11-01 | 2023-05-11 | ナチュラル オーシャン ウェル カンパニー | Adhesively bonded water separation cartridge module |
JP7270873B2 (en) | 2019-11-01 | 2023-05-11 | ナチュラル オーシャン ウェル カンパニー | Submersible water desalination system with replaceable and dockable membrane modules |
US12097466B2 (en) * | 2019-11-01 | 2024-09-24 | Natural Ocean Well Co. | Submerged water desalination system pump lubricated with product water |
Also Published As
Publication number | Publication date |
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NZ735748A (en) | 2018-07-27 |
AU2018370379B2 (en) | 2024-06-06 |
US12102964B2 (en) | 2024-10-01 |
WO2019098856A2 (en) | 2019-05-23 |
US20210046422A1 (en) | 2021-02-18 |
WO2019098856A3 (en) | 2019-06-27 |
AU2018370379A1 (en) | 2020-03-19 |
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