Seawater desalination system and energy recovery apparatus

US2016016826A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2016016826-A1
Application numberUS-201414774011-A
CountryUS
Kind codeA1
Filing dateFeb 25, 2014
Priority dateMar 11, 2013
Publication dateJan 21, 2016
Grant date

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  2. Abstract

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  5. First independent claim

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Abstract

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An energy recovery apparatus usable in a seawater desalination system. The energy recovery apparatus includes a plurality of chambers to pressurize the seawater by pressure energy of the concentrated seawater by supply and discharging the concentrated seawater and the seawater, a first flowmeter for integrating a flow rate of the seawater or the concentrated seawater which flows into the chamber, a second flowmeter for integrating a flow rate of the seawater or the concentrated seawater discharged from the chamber, a switching valve in each of the chambers to switch the inflow and the discharge of the concentrated seawater, and a controller to control the respective switching valves of the chambers on the basis of integrated flow rate of the chamber obtained from the flow rate of the flowmeter. The controller inputs a single input signal to the respective switching valves of the chambers to control the respective switching valves.

First claim

Opening claim text (preview).

1 . An energy recovery apparatus for exchanging pressure energy between concentrated seawater discharged from a reverse-osmosis membrane-separation apparatus and a part of seawater to be treated by the reverse-osmosis membrane-separation apparatus in a seawater desalination system for producing fresh water from the seawater by supplying the seawater to the reverse-osmosis membrane-separation apparatus to separate the seawater into fresh water and concentrated seawater, the energy recovery apparatus comprising: a plurality of chambers configured to pressurize the seawater by pressure energy of the concentrated seawater by supply and discharging the concentrated seawater and the seawater; a first flowmeter used for integrating a flow rate of the seawater or the concentrated seawater which flows into the chamber; a second flowmeter used for integrating a flow rate of the seawater or the concentrated seawater discharged from the chamber; at least one switching valve provided in each of the plurality of chambers and configured to switch the inflow of the concentrated seawater to the chamber and the discharge of the concentrated seawater from the chamber; and a controller configured to control the respective switching valves of the plurality of chambers on the basis of integrated flow rate of the chamber, the integrated flow rate of the chamber being obtained on the basis of the flow rate of the first flowmeter and/or the second flowmeter; wherein the controller inputs a single input signal to the respective switching valves of the plurality of chambers to control the respective switching valves. 2 . The energy recovery apparatus according to claim 1 , wherein valve opening and switching time of each of the switching valves can be controlled by the single input signal. 3 . The energy recovery apparatus according to claim 1 , wherein a trapezoidal wave is used for the single input signal. 4 . The energy recovery apparatus according to claim 1 , wherein the valve opening of each of the respective switching valves is set so as to vary in response to the input signal based on a predetermined setting value. 5 . The energy recovery apparatus according to claim 1 , wherein the controller controls the switching valve so as to perform switching of the switching valve of the chamber when an integrated flow rate of the chamber by the first flowmeter or the second flowmeter reaches a predetermined value. 6 . The energy recovery apparatus according to claim 5 , wherein switching of the switching valve is performed by a value calculated from a predetermined ratio of the actual volume of the chamber. 7 . The energy recovery apparatus according to claim 1 , wherein the controller controls the flow rate of the concentrated seawater discharged from the chamber by comparing an integrated value of an inflow amount of the concentrated seawater to the chamber and an integrated value of a discharge amount of the concentrated seawater from the chamber. 8 . The energy recovery apparatus according to claim 1 , wherein the controller controls the switching valve so that an integrated value of the inflow amount of the seawater to the chamber is equal to or larger than an integrated value of the inflow amount of the concentrated seawater to the chamber. 9 . The energy recovery apparatus according to claim 1 , wherein the controller controls the respective switching valves so as to include a process for discharging the pressurized seawater from the plurality of chambers simultaneously. 10 . An energy recovery apparatus for exchanging pressure energy between concentrated seawater discharged from a reverse-osmosis membrane-separation apparatus and a part of seawater to be treated by the reverse-osmosis membrane-separation apparatus in a seawater desalination system for producing fresh water from the seawater by supplying the seawater to the reverse-osmosis membrane-separation apparatus to separate the seawater into fresh water and concentrated seawater, the energy recovery apparatus comprising: a plurality of chambers configured to pressurize the seawater by pressure energy of the concentrated seawater by supply and discharging the concentrated seawater and the seawater; at least one switching valve provided in each of the plurality of chambers and configured to switch the inflow of the concentrated seawater to the chamber and the discharge of the concentrated seawater from the chamber; and a controller configured to input a single input signal to the respective switching valves of the plurality of chambers to control the respective switching valves. 11 . A seawater desalination system for producing fresh water from seawater by supplying the seawater to a reverse-osmosis membrane-separation apparatus to separate the seawater into fresh water and concentrated seawater, the seawater desalination system comprising: an energy recovery apparatus according to claim 1 for exchanging pressure energy between the concentrated seawater discharged from the reverse-osmosis membrane-separation apparatus and a part of the seawater to be treated by the reverse-osmosis membrane-separation apparatus. 12 . An energy recovery apparatus for exchanging pressure energy between concentrated seawater discharged from a reverse-osmosis membrane-separation apparatus and a part of seawater to be treated by the reverse-osmosis membrane-separation apparatus in a seawater desalination system for producing fresh water from the seawater by supplying the seawater to the reverse-osmosis membrane-separation apparatus to separate the seawater into fresh water and concentrated seawater, the energy recovery apparatus comprising: a plurality of chambers configured to pressurize the seawater by pressure energy of the concentrated seawater by supply and discharging the concentrated seawater and the seawater; a first flowmeter used for integrating a flow rate of the seawater or the concentrated seawater which flows into the chamber; a second flowmeter used for integrating a flow rate of the seawater or the concentrated seawater discharged from the chamber; at least one switching valve provided in each of the plurality of chambers and configured to switch the inflow of the concentrated seawater to the chamber and the discharge of the concentrated seawater from the chamber; and a controller configured to control the respective switching valves of the plurality of chambers on the basis of comparison between integrated flow rates of the chambers, each of the integrated flow rates of the chambers being obtained on the basis of the flow rates of the first flowmeter and the second flowmeter; wherein the controller inputs an input signal to the respective switching valves of the plurality of chambers to control the respective switching valves. 13 . An energy recovery apparatus for exchanging pressure energy between concentrated seawater discharged from a reverse-osmosis membrane-separation apparatus and a part of seawater to be treated by the reverse-osmosis membrane-separation apparatus in a seawater desalination system for producing fresh water from the seawater by supplying the seawater to the reverse-osmosis membrane-separation apparatus to separate the seawater into fresh water and concentrated seawater, the energy recovery apparatus comprising: a plurality of chambers configured to pressurize the seawater by pressure energy of the concentrated seawater by supply and discharging the concentrated seawater and the seawater; a first flowmeter used for integrating a flow rate of the seawater or the concentrated seawater which flows into the chamber; a second flowmeter used for integrating a flow rate of the seawater or the con

Assignees

Inventors

Classifications

  • Control or steering systems not provided for elsewhere in subclass C02F · CPC title

  • Energy recovery · CPC title

  • Controlling or regulating · CPC title

  • Energy recovery · CPC title

  • Reverse-osmosis · CPC title

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What does patent US2016016826A1 cover?
An energy recovery apparatus usable in a seawater desalination system. The energy recovery apparatus includes a plurality of chambers to pressurize the seawater by pressure energy of the concentrated seawater by supply and discharging the concentrated seawater and the seawater, a first flowmeter for integrating a flow rate of the seawater or the concentrated seawater which flows into the chambe…
Who is the assignee on this patent?
Ebara Corp
What technology area does this patent fall under?
Primary CPC classification C02F1/441. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Jan 21 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).