ES2291150T1 - Sistemas y plantas moviles de desalinizacion y procedimientos para producir agua-desalinizada. - Google Patents

Sistemas y plantas moviles de desalinizacion y procedimientos para producir agua-desalinizada. Download PDF

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ES2291150T1
ES2291150T1 ES04817834T ES04817834T ES2291150T1 ES 2291150 T1 ES2291150 T1 ES 2291150T1 ES 04817834 T ES04817834 T ES 04817834T ES 04817834 T ES04817834 T ES 04817834T ES 2291150 T1 ES2291150 T1 ES 2291150T1
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water
concentrate
discharge
intake
filtrate
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ES2291150T3 (es
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Andrew W. Gordon
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Water Standard Co LLC
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    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63J—AUXILIARIES ON VESSELS
    • B63J1/00—Arrangements of installations for producing fresh water, e.g. by evaporation and condensation of sea water
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025—Reverse osmosis; Hyperfiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/08—Apparatus therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/10—Accessories; Auxiliary operations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/12—Controlling or regulating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
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    • B01F25/421—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
    • B01F25/423—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components
    • B01F25/4231—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components using baffles
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
    • B01F25/452—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces
    • B01F25/4521—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces the components being pressed through orifices in elements, e.g. flat plates or cylinders, which obstruct the whole diameter of the tube
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    • C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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    • C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
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    • C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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    • 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
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/041—Treatment of water, waste water, or sewage by heating by distillation or evaporation by means of vapour compression
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F1/02—Treatment of water, waste water, or sewage by heating
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    • C02F1/06—Flash evaporation
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    • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
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    • C02F2103/08—Seawater, e.g. for desalination
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    • C02F2201/001—Build in apparatus for autonomous on board water supply and wastewater treatment (e.g. for aircrafts, cruiseships, oil drilling platforms, railway trains, space stations)
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    • C02F2201/008—Mobile apparatus and plants, e.g. mounted on a vehicle
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    • C02F2201/009—Apparatus with independent power supply, e.g. solar cells, windpower, fuel cells
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    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/005—Processes using a programmable logic controller [PLC]
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    • C02F2209/006—Processes using a programmable logic controller [PLC] comprising a software program or a logic diagram
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    • C02F2209/005—Processes using a programmable logic controller [PLC]
    • C02F2209/008—Processes using a programmable logic controller [PLC] comprising telecommunication features, e.g. modems or antennas
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    • C02F2303/24—Separation of coarse particles, e.g. by using sieves or screens
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    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • 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
    • 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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    • 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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    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract

Un buque que comprende: un sistema de purificación de agua que comprende: un sistema de admisión de agua que comprende una toma de agua y una bomba de admisión de agua, en el que la toma de agua es operable para disponerse encima de una región termoclina dentro de la masa de agua; un sistema de ósmosis inversa; un sistema de descarga de concentrado que comprende una pluralidad de puertos de descarga del concentrado; un sistema de transferencia del filtrado; una fuente de energía; y un sistema de control, en el que el sistema de ósmosis inversa está en comunicación con el sistema de admisión de agua, el sistema de descarga del concentrado y el sistema de transferencia del filtrado están en comunicación con el sistema de ósmosis inversa, y el sistema de control está en comunicación con el sistema de admisión de agua, el sistema de ósmosis inversa, el sistema de descarga del concentrado, el sistema de transferencia del filtrado y la fuente de energía; y en el que el sistema de descarga del concentrado comprende un miembro que es operable para extenderse desde el buque dentro o debajo de la región termoclina.

Claims (14)

1. Un buque que comprende:
un sistema de purificación de agua que comprende:
un sistema de admisión de agua que comprende una toma de agua y una bomba de admisión de agua, en el que
la toma de agua es operable para disponerse encima de una región termoclina dentro de la masa de agua;
un sistema de ósmosis inversa;
un sistema de descarga de concentrado que comprende una pluralidad de puertos de descarga del concentrado;
un sistema de transferencia del filtrado;
una fuente de energía; y
un sistema de control,
en el que
el sistema de ósmosis inversa está en comunicación con el sistema de admisión de agua,
el sistema de descarga del concentrado y el sistema de transferencia del filtrado están en comunicación con el sistema de ósmosis inversa, y
el sistema de control está en comunicación con el sistema de admisión de agua, el sistema de ósmosis inversa, el sistema de descarga del concentrado, el sistema de transferencia del filtrado y la fuente de energía; y
en el que
el sistema de descarga del concentrado comprende un miembro que es operable para extenderse desde el buque dentro o debajo de la región termoclina.
2. El buque de la reivindicación 1 en el que el sistema de descarga del concentrado comprende además un aspirador adecuado para extraer agua al interior del miembro de descarga desde la masa de agua circundante para la mezcla y subsiguiente disolución del concentrado antes de que el concentrado sea descargado a través de una pluralidad de puertos de descarga.
3. El buque de la reivindicación 1, en el que la toma de agua comprende un receptáculo marino.
4. Un buque que comprende:
un sistema de purificación de agua que comprende:
un sistema de admisión de agua que comprende una toma de agua y una bomba de admisión de agua;
un sistema de ósmosis inversa;
un sistema de descarga del concentrado que comprende una pluralidad de puertos de descarga del concentrado, en el que los puertos de descarga del concentrado funcionan para descargar el concentrado encima de una región termoclina de la masa de agua circundante;
un sistema de transferencia del filtrado que comprende una bomba de transferencia;
una fuente de energía; y
un sistema de control,
en el que
el sistema de ósmosis inversa está en comunicación con el sistema de admisión de agua,
el sistema de descarga del concentrado y el sistema de transferencia del filtrado están en comunicación con el sistema de ósmosis inversa,
la fuente de energía está en comunicación con el sistema de admisión de agua, el sistema de ósmosis inversa y el sistema de transferencia del filtrado, y
el sistema de control está en comunicación con el sistema de admisión de agua, el sistema de ósmosis inversa, es sistema de descarga del concentrado, el sistema de transferencia del filtrado y la fuente de energía; y
en el que
el sistema de admisión de agua comprende un miembro que es operable para extenderse desde el buque dentro o debajo de la región termoclina.
5. El buque de la reivindicación 4, en el que el sistema de descarga del concentrado comprende además un aspirador adecuado para extraer agua al interior del miembro de descarga desde la masa de agua circundante para la mezcla y subsiguiente disolución del concentrado antes de que el concentrado sea descargado a través de la pluralidad de puertos de descarga.
6. Un buque que comprende:
un sistema de purificación de agua que comprende:
un sistema de admisión de agua que comprende una toma de agua y una bomba de admisión de agua;
un sistema de ósmosis inversa;
un sistema de descarga del concentrado que comprende una pluralidad de puertos de descarga del concentrado;
un sistema de transferencia del filtrado;
una fuente de energía; y
un sistema de control,
en el que
el sistema de ósmosis inversa está en comunicación con el sistema de admisión de agua,
el sistema de descarga del concentrado y el sistema de transferencia del filtrado están en comunicación con el sistema de ósmosis inversa,
la fuente de energía está en comunicación con el sistema de admisión de agua, el sistema de ósmosis inversa y el sistema de transferencia del filtrado, y
el sistema de control está en comunicación con el sistema de admisión de agua, el sistema de ósmosis inversa, es sistema de descarga del concentrado, el sistema de transferencia del filtrado y la fuente de energía; y
en el que
el sistema de admisión de agua funciona para introducir el agua dentro del sistema de purificación de agua a una profundidad tal que se reduzca la introducción de plancton dentro del sistema de purificación de agua.
7. Un procedimiento para producir un filtrado sobre una estructura flotante que comprende:
la admisión del agua a través de un sistema de admisión de agua que comprende una toma de agua, en el que la toma de agua se dispone encima de una región termoclina de una masa de agua que circunda una estructura flotante;
el suministro del agua a un sistema de purificación de agua;
el filtrado del agua para producir un filtrado y un concentrado;
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la descarga del concentrado dentro de la masa de agua circundante a través de un sistema de descarga del concentrado que comprende un miembro de descarga que comprende una pluralidad de puertos de descarga del concentrado, en el que la pluralidad de puertos de descarga del concentrado se dispone dentro o debajo de la región termoclina.
8. El procedimiento de la reivindicación 7, que comprende además el paso de extraer agua al interior del miembro de descarga desde la masa de agua circundante a medida que el concentrado pasa a través del miembro de descarga.
9. Un procedimiento para producir un filtrado en una estructura flotante que comprende:
la admisión del agua a través de un sistema de admisión de agua que comprende un miembro de admisión de agua que se extiende desde el casco de la estructura flotante, en el que el miembro de admisión de agua comprende una toma de agua dispuesta encima de una región termoclina en una masa de agua que circunda una estructura flotante;
el suministro del agua a un sistema de purificación de agua;
el filtrado del agua para producir un filtrado y un concentrado;
la descarga del concentrado dentro de la masa de agua circundante a través de un sistema de descarga del concentrado que comprende un miembro de descarga que comprende una pluralidad de puertos de descarga del concentrado, en el que la pluralidad de puertos de descarga del concentrado se dispone dentro o debajo de la región termoclina.
10. El procedimiento de la reivindicación 9, que comprende además el paso de extraer agua al interior del miembro de descarga desde la masa de agua circundante a medida que el concentrado pasa a través del miembro de descarga.
11. Un procedimiento para producir un filtrado sobre una estructura flotante que comprende:
la admisión del agua a través de un sistema de admisión de agua que comprende un miembro de admisión de agua que se extiende desde el casco de la estructura flotante, en el que el miembro de admisión de agua comprende una toma de agua dispuesta dentro o debajo de una región termoclina en la masa de agua que circunda una estructura flotante;
el suministro del agua a un sistema de purificación de agua;
el filtrado del agua para producir un filtrado y un concentrado;
la descarga del concentrado dentro de la masa de agua circundante a través de un sistema de descarga del concentrado que comprende una pluralidad de puertos de descarga del concentrado, en el que la pluralidad de puertos de descarga del concentrado se dispone encima de la región termoclina.
12. El procedimiento de la reivindicación 11, en el que el sistema de descarga del concentrado comprende un miembro de descarga que comprende una pluralidad de puertos de descarga del concentrado.
13. El procedimiento de la reivindicación 12, que comprende además el paso de extraer agua al interior del miembro de descarga desde la masa de agua circundante a medida que el concentrado pasa a través del miembro de descarga.
14. Un procedimiento para producir un filtrado sobre una estructura flotante que comprende:
la admisión del agua a través de un sistema de admisión de agua que comprende una toma de agua, en el que la toma de agua se dispone a una profundidad por debajo de los 10 metros;
el suministro del agua a un sistema de purificación de agua;
el filtrado del agua para producir un filtrado y un concentrado;
la descarga del concentrado dentro de la masa de agua circundante a través de un sistema de descarga del concentrado que comprende una pluralidad de puertos de descarga del concentrado.
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CY1111044T1 (el) 2015-06-11
CN1890184A (zh) 2007-01-03
EP1697261A1 (en) 2006-09-06
US20080011681A1 (en) 2008-01-17
ATE459578T1 (de) 2010-03-15
CY2200154T2 (el) 2010-07-28
US20080173589A1 (en) 2008-07-24
TNSN06171A1 (en) 2007-11-15
KR20060123444A (ko) 2006-12-01
WO2005061389A1 (en) 2005-07-07
CA2548720A1 (en) 2005-07-07
NI200600129A (es) 2007-04-10
EP1697261B1 (en) 2010-03-03
US7416666B2 (en) 2008-08-26
NO20063344L (no) 2006-09-15
ES2291150T3 (es) 2010-06-30
DE602004025848D1 (de) 2010-04-15
CN1890184B (zh) 2010-05-26
RU2006124355A (ru) 2008-01-20
US20040206681A1 (en) 2004-10-21
ZA200605694B (en) 2007-10-31
US7476323B2 (en) 2009-01-13
BRPI0417121A (pt) 2007-03-06
IL176226A0 (en) 2006-10-05
BRPI0417121B1 (pt) 2014-02-18
US20080011689A1 (en) 2008-01-17
AP2006003692A0 (en) 2006-08-31
CO5720990A2 (es) 2007-01-31
AU2004303800A1 (en) 2005-07-07
JP2007513759A (ja) 2007-05-31
EG24347A (en) 2009-02-12
AU2004303800B2 (en) 2010-08-19
MA28281A1 (fr) 2006-11-01

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