Fluid exchanger devices, pressure exchangers, and related methods
US-9435354-B2 · Sep 6, 2016 · US
US2019366271A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2019366271-A1 |
| Application number | US-201716463496-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 22, 2017 |
| Priority date | Nov 24, 2016 |
| Publication date | Dec 5, 2019 |
| Grant date | — |
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A system for purifying a treated liquid, including: a treatment module, for treating the liquid and providing a purified liquid, and a residual liquid; and a means for pressurizing said treated liquid to supply said treatment module, including: a master cylinder, driven by a working fluid, and at least slave cylinder, driven by said master cylinder, receiving said treated liquid and supplying it to said treatment module; a cross section of said master cylinder is greater than a cross section of said slave cylinder so that, a greater pressure is generated on the treated liquid in the slave cylinder; and a means for pre-pressurizing the treated liquid, upstream of the pressurizing means, including: at least one master cylinder, connected to the treatment module, and driven by the residual liquid, and a slave cylinder, containing the treated liquid, driven by said master cylinder.
Opening claim text (preview).
1 . A system for purifying a liquid, called liquid to be treated, in particular salt water, comprising: a module, called treatment module, for treating the liquid to be treated and providing on the one hand a liquid, called purified liquid, and on the other hand a liquid, called residual liquid; and a means for pressurizing said liquid to be treated in order to supply said treatment module, comprising: a cylinder, called master cylinder, provided to be driven by a fluid, called working fluid; and at least one cylinder, called slave cylinder, driven by said master cylinder, provided to receive said liquid to be treated and supply it to said treatment module; a cross section of said master cylinder is greater than a cross section of said at least one slave cylinder so that, for a given pressure of said working fluid in the master cylinder, a greater pressure is generated on the liquid to be treated in the slave cylinder; and a means for pre-pressurizing the liquid to be treated, upstream of the pressurizing means; said pre-pressurizing means comprising: at least one cylinder. called master cylinder, connected to the treatment module, and driven by the residual liquid provided by the treatment module; and a cylinder, called slave cylinder, containing the liquid to be treated, driven by said at least one master cylinder. 2 . The system according to claim 1 , characterized in that the treatment module is a module for treating liquid to be treated by reverse osmosis. 3 . The system according to claim 1 , characterized in that the master cylinder is a double-acting cylinder, and the pressurizing means comprises two slave cylinders, situated symmetrically on both sides of the master cylinder, and driven by said master cylinder. 4 . The system according to claim 1 , characterized in that it comprises a reservoir, called intermediate reservoir arranged in order to store the liquid to be treated at an intermediate pressure, less than the osmotic pressure, at the outlet of the means for pre-pressurizing the liquid to be treated and in order to supply the pressurizing means with liquid to be treated. 5 . The system according to claim 1 , characterized in that the working fluid is a thermal fluid, the pressure of which varies as a function of its temperature, said system comprising a thermal device, arranged upstream of the pressurizing means, and carrying out a heat exchange towards said working fluid, so as to increase its pressure. 6 . The system according to claim 1 , characterized in that the working fluid is an incompressible fluid, said system comprising: a thermal device, arranged upstream of the pressurizing means, and carrying out a heat exchange towards a thermal fluid, so as to increase the pressure of said thermal fluid; and a pressure transfer means, arranged between said thermal device and the pressurizing means, in order to transmit the pressure from said thermal fluid to the working fluid. 7 . The system according to claim 6 , characterized in that the pressure transfer means comprises: at least one cylinder, called transfer cylinder, connected to the pressurizing means, and provided to receive the working fluid; and at least one deformable volume, arranged in said transfer cylinder, and provided to receive the thermal fluid. 8 . The system according to claim 5 , characterized in that the thermal fluid is selected from the saturated or unsaturated C5- to C10-type hydrocarbons, or from the organic fluids (R134a, R236fa, R254fa, R600, R601, RC318, R1234yf) or mixtures of azeotropic or non-azeotropic organic fluids. 9 . The system according to claim 5 , characterized in that it comprises a thermal fluid pre-pressurizing means, arranged upstream of the thermal device. 10 . The system according to claim 9 , characterized in that the thermal fluid pre-pressurizing means comprises: at least one cylinder, called master cylinder, driven by the residual liquid provided by the treatment module; and a cylinder, called slave cylinder, containing the thermal fluid, driven by said at least one master cylinder. 11 . A method for purifying a liquid, called liquid to be treated, in particular salt water, comprising at least one iteration of the following steps: pressurizing the liquid to be treated; supplying said pressurized liquid to be treated to a treatment module providing a first liquid, called purified liquid, and a second liquid, so-called residual liquid; the pressurizing step is carried out by at least one cylinder, called slave cylinder, firmly connected to a cylinder, called master cylinder, with a cross section larger than the cross section of said slave cylinder, and receiving a working fluid; and a step of pre-pressurizing the liquid to be treated, before the step of pressurizing the liquid to be treated, carried out by a cylinder, called slave cylinder, containing the liquid to be treated, firmly connected to at least one cylinder, called master cylinder, receiving the residual liquid. 12 . The method according to claim 11 , characterized in that the treatment module is a module for treating liquid to be treated by reverse osmosis. 13 . The method according to claim 11 , characterized in that the master cylinder is a double-acting cylinder, and drives two slave cylinders so that, when one of the slave cylinders is emptied of liquid to be treated, the other slave cylinder is simultaneously filled with liquid to be treated. 14 . The method according to claim 11 , characterized in that the working fluid is a thermal fluid, said method comprising a step of increasing the pressure of said working fluid by heat exchange. 15 . The method according to claim 11 , characterized in that the working fluid is an incompressible fluid, said method comprising the following steps: a step of heat exchange towards a thermal fluid in order to increase the pressure of said thermal fluid; and a step of transferring pressure from said thermal fluid to said working fluid. 16 . The method according to claim 15 , characterized in that the pressure transfer step is carried out by at least one cylinder containing the working fluid and an elastic bladder, arranged in said cylinder, and containing the thermal fluid. 17 . The method according to claim 14 , characterized in that it comprises a step of pre-pressurizing the thermal fluid, carried out by a cylinder, called slave cylinder, containing the thermal fluid, firmly connected to at least one cylinder, called master cylinder, receiving the residual liquid. 18 . The method according to claim 15 , characterized in that it comprises two half cycles, each half cycle comprising the following phases: a phase I simultaneously comprising: a step of increasing the pressure of the thermal fluid by heat exchange; and a step of transferring pressure from said thermal fluid to said working fluid; a phase II simultaneously comprising: a step of increasing the pressure of the thermal fluid by heat exchange; a step of transferring pressure from said thermal fluid to said working fluid; a step of pressurizing the liquid to be treated; a step of purifying the liquid to be treated by reverse osmosis; and a step of pre-pressurizing the thermal fluid; a phase III simultaneously comprising: a step of increasing the pressure of the thermal fluid by heat exchange; a step of transferring pressure from said thermal fluid to said working fluid; a step of pressurizing the liquid to be treated; a step of purifying the liquid to be treated by reverse osmosis; and a step of pre-pressuriz
with two mechanically connected pumping members · CPC title
Accessories; Auxiliary operations · CPC title
Specific pressurizing or depressurizing means · CPC title
Construction details of the apparatus · CPC title
by reverse osmosis · CPC title
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