MX347833B - Procedimiento de suministro de agua de salinidad controlada. - Google Patents

Procedimiento de suministro de agua de salinidad controlada.

Info

Publication number
MX347833B
MX347833B MX2012008177A MX2012008177A MX347833B MX 347833 B MX347833 B MX 347833B MX 2012008177 A MX2012008177 A MX 2012008177A MX 2012008177 A MX2012008177 A MX 2012008177A MX 347833 B MX347833 B MX 347833B
Authority
MX
Mexico
Prior art keywords
ppm
membrane units
range
feed water
permeate
Prior art date
Application number
MX2012008177A
Other languages
English (en)
Other versions
MX2012008177A (es
Inventor
Dale Williams John
Original Assignee
Bp Exploration Operating
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.)
Filing date
Publication date
Application filed by Bp Exploration Operating filed Critical Bp Exploration Operating
Publication of MX2012008177A publication Critical patent/MX2012008177A/es
Publication of MX347833B publication Critical patent/MX347833B/es

Links

Classifications

    • 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
    • B01D61/029—Multistep processes comprising different kinds of membrane processes selected from reverse osmosis, hyperfiltration or nanofiltration
    • 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
    • B01D61/06—Energy recovery
    • 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
    • B01D61/026—Reverse osmosis; Hyperfiltration comprising multiple reverse osmosis steps
    • 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
    • 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
    • B01D61/58—Multistep processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/10—Spiral-wound membrane modules
    • B01D63/12—Spiral-wound membrane modules comprising multiple spiral-wound assemblies
    • 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
    • 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
    • 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
    • C02F1/442—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2311/00—Details relating to membrane separation process operations and control
    • B01D2311/14—Pressure control
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2311/00—Details relating to membrane separation process operations and control
    • B01D2311/16—Flow or flux control
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2317/00—Membrane module arrangements within a plant or an apparatus
    • B01D2317/04—Elements in parallel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2317/00—Membrane module arrangements within a plant or an apparatus
    • B01D2317/08—Use of membrane modules of different kinds
    • 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
    • B01D61/027—Nanofiltration
    • 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
    • C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/101—Sulfur compounds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08—Seawater, e.g. for desalination
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/05—Conductivity or salinity
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/40—Liquid flow rate
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00—General aspects of water treatment
    • C02F2301/04—Flow arrangements
    • C02F2301/043—Treatment of partial or bypass streams
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/10—Energy recovery
    • 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
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/30—Wastewater or sewage treatment systems using renewable energies

Abstract

Un procedimiento de producción de una corriente de agua de inyección de salinidad controlada y contenido en aniones sulfato controlado que es adecuada para inyección en una formación petrolífera de un yacimiento petrolífero, comprendiendo el procedimiento las etapas de: (a) alimentar un agua de origen que tiene un contenido en sólidos disueltos totales en el intervalo de 20.000 a 45.000 ppm y una concentración de aniones sulfato en el intervalo de 1.000 a 4.000 ppm, preferiblemente de 1.500 ppm a 4.000 ppm a una planta de desalinización que comprende una pluralidad de unidades de membrana de ósmosis inversa (OI) y una pluralidad de unidades de membrana de nanofiltración (NF), en el que el agua de origen se presuriza hasta una presión en el intervalo de 350 a 1250 psi absolutas, y dividir el agua de origen para proporcionar un agua de alimentación para las unidades de membrana de OI (en lo sucesivo en el presente documento "agua de alimentación de OI") y un agua de alimentación para las unidades de membrana de NF (en lo sucesivo en el presente documento "agua de alimentación de NF"); (b) si es necesario, aumentar la presión del agua de alimentación de OI hasta un valor en el intervalo de 900 a 1250 psi absolutas antes de introducir el agua de alimentación de OI en las unidades de membrana de OI y retirar un material permeado de OI y un material retenido de 01 de las unidades de membrana de 01, en el que las unidades de membrana de OI se hacen funcionar o bien en un modo de paso único, fase única o bien en un modo de paso único, dos fases y en el que la recuperación de material permeado de OI está en el intervalo del 35 al 75% en volumen, preferiblemente del 35 al 60% en volumen basado en el volumen del agua de alimentación de OI que se alimenta a las unidades de membrana de OI, de manera que el material permeado de OI tiene un contenido en sólidos disueltos totales inferior a 250 ppm, y una concentración de aniones sulfato inferior a 3 pprn; (c) si es necesario, reducir la presión del agua de alimentación de NF hasta un valor en el intervalo de 350 a 450 psi absolutas antes de introducir el agua de alimentación de NF en las unidades de membrana de NF y retirar un material permeado de NF y un material retenido de NF de las unidades de membrana de NF, en el que las unidades de membrana de NF se hacen funcionar en un modo de paso único, fase única y en el que las unidades de membrana de NF se hacen funcionar con una recuperación de material permeado de NF en el intervalo del 35 al 60% en volumen basado en el volumen del agua de alimentación de NF que se alimenta a las unidades de membrana de NF, de manera que el material permeado de NF tiene un contenido en sólidos disueltos totales en el intervalo de 15.000 a 40.000 ppm, preferiblemente de 15.000 a 35.000 ppm, y una concentración de aniones sulfato inferior a 40 ppm, preferiblemente inferior a 30 ppm; y (d) mezclar al menos una parte del material permeado de OI y al menos una parte del material permeado de NF en una razón en el intervalo de 2:1 a 40:1, preferiblemente de 4:1 a 27:1, en particular de 10:1 a 25:1 para proporcionar un agua de inyección que tiene un contenido en sólidos disueltos totales en el intervalo de 500 a 5.000 ppm, y una concentración de aniones sulfato inferior a 7,5 ppm, preferiblemente inferior a (5) ppm, más preferiblemente inferior a 3 ppm.
MX2012008177A 2010-01-14 2011-01-11 Procedimiento de suministro de agua de salinidad controlada. MX347833B (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP10250063 2010-01-14
PCT/GB2011/000032 WO2011086346A1 (en) 2010-01-14 2011-01-11 Process of supplying water of controlled salinity

Publications (2)

Publication Number Publication Date
MX2012008177A MX2012008177A (es) 2012-10-01
MX347833B true MX347833B (es) 2017-05-12

Family

ID=42173278

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2012008177A MX347833B (es) 2010-01-14 2011-01-11 Procedimiento de suministro de agua de salinidad controlada.

Country Status (9)

Country Link
US (2) US9492790B2 (es)
EP (1) EP2523908B1 (es)
CN (1) CN102803148B (es)
AU (1) AU2011206433B2 (es)
BR (1) BR112012017561B1 (es)
CA (1) CA2786348C (es)
EA (1) EA025116B1 (es)
MX (1) MX347833B (es)
WO (1) WO2011086346A1 (es)

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Also Published As

Publication number Publication date
US9492790B2 (en) 2016-11-15
CA2786348A1 (en) 2011-07-21
EP2523908B1 (en) 2018-10-24
US9555373B2 (en) 2017-01-31
WO2011086346A1 (en) 2011-07-21
CN102803148B (zh) 2015-07-22
AU2011206433A1 (en) 2012-07-19
AU2011206433B2 (en) 2015-02-12
US20150083656A1 (en) 2015-03-26
US20120261340A1 (en) 2012-10-18
EA201201005A1 (ru) 2013-02-28
CA2786348C (en) 2018-04-03
BR112012017561A2 (pt) 2016-08-16
CN102803148A (zh) 2012-11-28
EA025116B1 (ru) 2016-11-30
EP2523908A1 (en) 2012-11-21
MX2012008177A (es) 2012-10-01
BR112012017561B1 (pt) 2019-12-03

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