SA99200315B1 - The reverse osmosis desalination plant is equipped with pressurized tanks with a continuous kinetic cycle. - Google Patents

Abstract

Comprises at least one auxiliary pump(1) and a high pressure pump(2) in parallel with an ‎internal circulation pump(3) and at least one pair of mother chambers(5 and 5’) which ‎became alternatively pressurized, each forming a preferably toroidal closed circuit, in ‎amanner that the water always circulates in the same direction without stopping , taking ‎advantage of its kinetic energy during valve changes being liable to be fitted with a ‎means of separation between water masses having different salinity levels in the form of ‎sphere-shaped pistons ( 7 and 7’) with an appetent density similar to that of the water, ‎which pistons are briefly detained in the course of cycle changes by baskets(6 and 6’) or ‎equivalent devises while the water continues to circulate at the expense of its kinetic ‎energy, the cycle changes being controlled either by approaching (29 and 29’) and ‎lodging (28 and 28’) sensors or by flow meters(31 and 31’ and 32) or else by salinity ‎measurements in the event that said separation means are not fitted , Fig 1‎

Description

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With tanks 33 5 4 reverse osmosis Pressurized reverse osmosis water desalination plant with continuous kinetic cycle Full description: Background of the invention Desalinating water system The invention relates to a system Provides features related to pressurized chambers inverse osmosis small size and size functionality cenergy consumption .emptying and emptying water filling speed of chambers by increasing the speed © Spanish patent application No. 9701897 in the name of the same applicant describes mother chambers Reverse osmosis desalination with mother chambers The current unit is a unit of water masses to separate piston blocks inside which a piston rotates compressed into cylinders However, it was noticed that it is in a different fan state. Although the operation of the unit is satisfactory salinity with salinity it is not advisable to reverse the movement of large-size facilities large-size facilities 0 pressure for parent chambers in view of energy cycles water and piston at the end of all large-size facilities kinetic energy: general description of the invention substantial; Specifically, the diay cycle, and the present invention is based on a different principle by which water masses of different salinities, which have a continuous kinetic cycle, rotate through the parent chamber always in the same direction, without stopping; So that dissipating the kinetic energy of the moving water mass and then accelerating it in the opposite direction becomes unnecessary. This leads to improved equipment life and reliability; significant energy savings; reduction in chamber volume; reliability

RR v is longer. The system is distinguished first and foremost in that the two pressurized parent equipment or compartments used to store water from which desalination should be no longer formed in the equipment and may or may not be provided with a piston to separate the water from the straight-line tube Picture of a straight tube, and the chamber described in this statement below is a brine, from which the salt and brine water should be removed, so that it connects the beginning and the end of the tube, thus forming a ring-shaped circle in the form of a zigzag ring or in the form of a toroidal zigzag The tube shall be in the form of a closed circuit or otherwise shaped; It does not matter how strange or functional it is; the helicoidal is continuous or helical and the only requirement is that its beginning and end be connected to form a loop or a closed loop. The aforementioned piston is able to rotate along the lines ai Soy like a ball of water and that esphere-shaped spherical shape © water; So that the density is approximately equal to the density and weight of the connected pipe and its weight is centrifuged curves can be drawn into the flow and will not be separated by centrifugation (plastic and metal Jie due to its excessive density Any material such as that found in the elastic daw (Says 2) can be used. And it is able to resist wet when wet. Tan has little friction. ve may form light ewalls with walls impacts sufficiently directional changes or bumps elastomers or rubber materials or rubber monomers gels as well as by accumulating gels silicone materials 165 used in members (Jie low-hardness low hardness hollow rubber ball or even a mammary prostheses mammary prostheses simple enough to accommodate a simple resiliency filled with water or a small amount of some other substance that provides it with bounce > route or stopping the ball or piston where the recovery is installed and the third feature of the retrieval technique is to receive the ball and send it back along the same baseball glove with a non-return valve design through a fluid bypass tract; With a fluid bypass: for water in such a way that when the water inlet is closed to a special inertia that opens by inertia ve

The compartment The mass that rotates inside the chamber is not constrained but is free to rotate inside the ring in exchange for the loss of kinetic energy in the mass (AS jana) which should not be stopped and then put into Als motion as in Ula alternating motion piston calternate movement piston The only element that should be stopped is the small mass of the ball-shaped piston if supplied. The system also includes valves; Pumps and a cpiston-position detecting system, all operated in a programmed fashion to obtain the desired result. To solve the above problems; Tal has incorporated several improvements in its reverse osmosis (RO) desalination units that include main chambers with a continuous cycle; mS J greatly simplifies its practical embodiment without modifying the aforementioned operation principles. The first improvement lies in the addition of two three-way slide valves mechanically coupled to each other. The normal and simple requirement for a vo valve of a three-way slide valve type with a cylinder and radial ports is that the slide valve shall be provided with a single groove and for the main intake of the three port lines the common inlet or outlet shall be ; so that when the slide valve is at an end; The ports on that side are connected 3S Hall ¢ and when on the other end the other side is also connected to the center. The described Gana six-way double-groove valve has a problem in that the times required for filling and emptying the parent chambers are not uniform; Thus, the sizes to be processed in the first compartment and the second compartment are different. This is because the sequence of closing and opening times is not the same in each compartment; Since in order to close the first compartment, the second compartment must be opened; During this timeframe the second compartment should open and close so the vo time for this second compartment becomes much shorter. There are two means to solve this problem: The first solution lies

In providing one of these three-way valves with a double groove for reversing operation; That is, the ports that were open in the first case are now closed, and vice versa; The second solution is to divide the valve into six lanes. any; double group of three yan and reversing the operating direction of one group with respect to the other. This second solution entails the use of a mechanism 0 that provides movement for one of the slide valves in one direction while the other slide valve moves in the opposite direction. This justifies the choice of two valves With three passages, one of which is provided with a double-segment slide valve, although more can be said in this regard. The valves are provided with a double sleeve or an external housing that defines multiple collecting chambers for these outlets, separated from each other by means of annular separators. These chambers play an important role in this system, not only in terms of Relates to the manifold that connects the outer connections to the corresponding outlets; but in that it allows water to pass from the parent compartments

. when the spin valves open; The water from the mother chambers is able to circulate in a continuous kinetic cycle; This means that when fluid is trapped because the valves are closed in relation to the outside; The recirculation valves open as a result of kinetic energy as the water rotates over itself in an Allie ring thus eliminating ramming and keeping the water mass in motion until the next direct process occurs.

1 The second improvement is to depressurize the main chambers before unloading the brackish water out; This increases the service life of recirculating valves so that they can be operated in a less demanding manner. This previous depressurization is accomplished through small-section tan ports that open directly before the main discharge ports.

As it is known, Ad dua, there are many ways to operate the different types of valves (LZ of (Aa idl Yo) hydraulically or mechanically emechanical.

+ Its positioning is a problem in the presence of numeric control computer systems, stepper motors and similar tools currently available. Thus, the third improvement lies in the combination of a very simple mechanical driving mechanism, which is operated by means of a fixed angular motion shaft, such as an electric motor shaft, through an e-speed reduction box, and works to stop slides of the valves at each end when the parent chambers are filled or emptied and additionally promise a soft stop or low speed at a point in their stroke corresponding to the 'pre-press' operation; As described in Spanish Patent Application No. AA AA this (pT Say) main chambers of high pressure retaining diaphragms -0 cmembranes and perform the rest of the stroke as quickly as possible. This can be achieved by means of a combination of planetary gears. planetary gears of 5 diameters suitable for moving any point of the planetary gears through an epicycloid trajectory and inside the valves the water undergoes changes in direction Italia which make the flow turbulent to the point of cle and this is most likely to happen if the water flows Relatively high speed JED designed valves size.However, to remove the moving pistons Gy of the previous technology, the flow should be as laminar as possible to avoid deformation of the surface separating water masses that have excessively different salinity levels, which leads to mixing of the masses The goal of the fourth improvement is to reduce turbulence, and this is achieved by placing thin plates (laminators) in the flow at the valve outlets.

1800044 in each of Spain's patent applications Nos. 43600744 and No. 1 and in the initial concept of continuous motor cycle main compartments; use between tubes; Valves T° connections Tan connections are a large number

And the mother's cubicles. This compromises the hydrodynamics of the system. In this case this problem is greatly reduced. Using separate valves for each process is more costly and more difficult to synchronize than using a single six-way valve. This solution can be further improved if the system is equipped with two double-sleeve three-way valves, ie with two bodies The two cylinders are concentric; and they operate at the same time. This improves the hydrodynamics of the fluid; as well as facilitating access to the various parts for the purposes of maintenance or repair of the assembly as all the valves are combined in a Tan made design so that they can be reduced in size and provide a final design Acceptable appearance Ve and effective It should be remembered that VE requires a valve consisting of: mechanically driven valves (Jal when Td two units with three passages); one-way non-return valves two recirculating valves per chamber (constituting These two valves are the main element in the system to prevent fluid lag and to complete the continuous motor cycle): two prepressure valves and two prepressure reducing valves.LY vo Low production costs raw material and labor costs Significantly improved access to the various parts “replacement Jai wD” repair or maintenance; Above all; The full range of desalting unit process valves can easily be transported with pipework and pumps hook-ups performed on-site only. GIG's solution to the non-operational BLS problem caused by the six-pass valve is that this valve; (Chay WS) entails that each of the two parent chambers be provided with different operating times and therefore different sizes. To complete this description and to assist in better understanding the characteristics of the invention, a detailed description of a preferred embodiment based on a set of drawings is attached hereto ARR

A

The following description is for guidance only and is not 54) integra. part, which forms an integral part to reduce the invention. A brief explanation of the drawings: A schematic drawing showing the steps of the system operation at a certain point in the cycle; at the end of its process ° from which desalination should be made to a membrane; It is almost filled with brine and divided by a piston in the shape of a striped zone. At the same time, the sphere-shaped piston. The lower sphere has emptied its contents of brine and is now completely enclosed. It can be noted that the piston in the shape of a sphere 1 with its open part being 'U' through a basket in the form of a letter pen force, and it is also clear that the force 0 directed to the right to receive the water piston has opened a valve Along the sideways stream so that the water flow did not stop.: Shows the same system shown in the previous figure in a case where the basket of the compartment 1 rotated Figure vo _ to enable the piston to follow its path from right to left. The first 081 is considered This is an operational step whereby both compartments simultaneously supply their content to the membrane. Now with brine water; the basket is collected. Figure LIS?: Shows that the first chamber is full of the piston and that the brine flow has opened the valve Lateral, while 0: for brine 1 in collecting water i the lower chamber provides new water to the membrane and the extruded water appears with the brine water being sent out; Jal The lower chamber supplies water to the membrane while collecting brine water from the right side of the piston.

Figures © through 10: show a temporary operation sequence in a modified version to collect an alternative piston called the concealment sequence. 0 Figures 11 through 60: show an operation sequence Temporary in a modified version of the alternate piston collection it is called the double piston sequence. Juss from Ye to 18: correspond to the same moments in the cycle shown in figures 1 to ; It shows a change of 0 in the system where the separator piston is not supplied. Figures 19 through YY: show the same circuit; Same principle and same operation although this may not be obvious because the drawing has been treated differently. The only difference is that the water load is determined to be greater or less depending on the circuit diameters. The objective of 1s is to prevent a chamber which converges to form a loop from having the same diameter through its path in such a manner that one length may be supplied with one diameter and another length may be supplied which closes the circuit and provides a non-return valve; with different diameter; It may also have many lengths with different diameters without affecting the operating principle of the system in the least. YY Ja Y. : shows a schematic view of the desalting unit assembly according to the invention. Figure YY: shows a schematic plan view of the two valves with three passages. Figure Ye Dippin My hometown elevation section of the previous Yo schematic view. 0 no

Ve

Jus zy) several Jal je cycle: showing the arrangement of the valves and the flow of various fluids in 1 to YO from the desalting unit. of the desalting unit according to the invention. bottom view cpa TY The figure of the desalination unit according to the invention. Semi-sectional view of the elevation unit shows the semi-sectional view of my hometown ve the figure of the invention. Gy Desalting unit: shows a horizontal projection view of the desalting unit according to the invention. An overlying cycloid at the right end of its stroke. Figure +0 shows a schematic view of an overlying cyclic operation at the beginning of its useful stroke. Tyla: A schematic view of an overlying cyclic operation at the point where the chamber is compressed. cpu YA Preformed first parent compartment. Reduces Cus pressure: Shows a schematic view of a supracyclic operation at point va Figure prefixed the second parent compartment. Figure £0 two defects Schematic view of an epicyclic operation at the end Its useful stroke. 6 for a thin plate in flow. sheet lattice design (Sul) Figure 61 shows the design of a radial sheet in flow and a concentric tube. Figure 7 shows a diagonal lattice concentric tube Fig. 47 Detailed description: 7 to 47; brine water represented as dark regions; raw water YT in figures from without dark region The white arrows represent low pressure; While the black arrows represent high pressure. The recirculating and non-return valves are shown in black when closed or white when opened

ARR

1 The innovative system includes two chambers in the form of 5 9 7; The position of the pistons partitions ag ( Y4 5 Yq) of the piston approach sensors is determined by means of two lodging sensors (0 + stability of the piston (YA) and 78). The two barriers (01 and 10) act as protective devices (TAs A) to avoid the possible tendency of the pistons to direct them through two protections. The two baskets (+ and ); The two molds are in the shape of the letter “L” with the open part oriented and the base (VV) provided to the left or right; The two baskets with two small non-return valves (V4) aie (Fe 71) and the mentioned chambers (0 and *') receive the water to be desalinated 1

VY) by means of the two non-return valves (1) auxiliary pump supplied from an auxiliary pump (1 and 1”). When the valves (VY) open and the internal circulation pump (©) supplies water to the chambers (0) and (© ) and to the diaphragm (£) by means of the two non-return valves (?1) and (?1). vo pump (Y) is a main or high-pressure pump providing the diaphragm (£) with a controlled flow that shall be executed through The membrane and then leaves the system in the form of produced water (71). The operation is as follows: Tey from the position shown in Figure 1 and precisely any point in the cycle; indicates the arrival of the piston (7) and the chamber (*) to the end Their stroke as they are about to alert the piston approach sensor (YR) - © while the brine water thrown behind the piston passes the diaphragm ball (4) through the return conductor (© 7); and passes through the open brine inlet valve (WY) through the inlet stream (V1) enters the chamber and fills it with brine (bare area) and forces the remaining water to be desalted into said chamber to the left of the plunger (7); shown in white background (no lines This water is then sucked out by means of: the internal circulation pump (7) and leaves the chamber by way of the outlet chute (71); pass Elsie vo 0 a

VY

non-return valve (£1)« and is sucked through the pressurized conduit (77) by means of the internal circulation pump (7); and through the common conduit (16) it enters the diaphragm via the diaphragm conduit (77). This water does not pass through the diaphragm because it circulates in A closed circuit whose task is to withdraw the salts left by the water and remaining in the membrane, and this depends entirely on the pump, le 0 | pressure (7), and provided that the pressure in the high-pressure pump (7) does not exceed the permeating pressure. Saline matter remains in the membrane, and the function of the internal circulation pump (7) is to circulate water only in a closed circuit between the membrane and the chambers.As noted, the basket (1) for receiving the piston (V) is not in position to receive it, because In the opposite direction, specifically towards the left of the drawing, while the piston protrudes from the right side. The piston ('YA) lodging sensor positions the piston ('V) and closes the unloading valve ('YY) unloading valve and separates the water supplied by the auxiliary pump (1) and the stream conduct (YY) of the ('V¥) non-return valve and entry conductor (11) oe. Since the water in this chamber circulates clockwise; It is when the unloading valve (VY) closes suddenly; The water inside the chamber tries to continue circulating in the same way for a short period of time; The force exerted by this mass, in exchange for the loss of fluid kinetic energy, causes the water to branch off through the bypass conductor ('A) and to open the bypass valve (4). “” while the pressure vy. pressing valve (© (1) opens and pressurizes the chamber (10) via the pressurizing conductor (©7’) at the pressure supplied by the high-pressure pump circuit ( Y) high pressure pump, which so far reaches atmospheric pressure, but at this moment is equal to the prevailing pressure in the chamber (0) and while old the piston (V) passes in the chamber (*) shown in the figure? through a piston vo piston approach sensor (79); which commands the basket (1) to rotate 081

degrees, while the brine entry valve “(‘11) opens as shown in Figure Y. Baskets (7) and (11) are provided with two small non-return valves (V0) and (71) on the part opposite its open entrance in the same way as the side valves (3) and (9') are supplied, as a result of the kinetic energy of the fluid generated from the part opposite the entry point of the pistons (7) and (7), specifically the back side. So that the piston comes out of the basket (1) and is positioned so that it is pushed through the brine water coming from the membrane (;) and through the internal circulation pump (Y) through the return stream (; 7) and the brine water inlet valve ( MY) which has opened now. This is an important period of time for the system, as the two chambers work in parallel; (10) ready for operationalal operation only. This simultaneous operation is necessary to avoid sudden chamber changes, thus avoiding exposure of the diaphragm to sudden pressure changes. When the piston (7) reaches the basket (1); As shown in the figure Sa oF compartment 1 (0) (striped zone) with brine water. At this point, as in the case of compartment (©'); which Sa is with the water from which desalination is to be made; The pressure exerted against the loss of kinetic energy by means of counter-clockwise rotating brine A opens the valve (3) in a bypass (A) and is momentarily set in motion without block stopping fluid; for a long period of time sufficient to affect the discharge valve (VY) which is still © - closed until now (Fig. oF) and opens as shown in Fig. At this moment, the basket (11) is oriented towards the left of the drawing to release the piston as shown in Figure 4. As can be seen, this process is a single process where the two chambers (*) and (5) contribute their contents to the Gy membrane of an alternate sequence and the brine is collected The projected reject brine is in the ve opposite side of the pistons (7) and (TY) The important aspect of this system is that the water movement ARK

Continuous Lyi with only a slight pause in the valve change process; which may be quick as needed; While the water in the chamber continues to circulate. Therefore; The positive and negative forces of acceleration and deceleration of the moving liquid mass 85 inside the chambers can be neglected.

o Having described the embodiment and operation of the system to which the invention is intended; A series of changes and substitutions may appear to a person expert in this subject without changing the principle of operation of the system” and thus becoming more adapted to the special requirements that he believes to be contained in the elements of the protections of this patent.

Likewise, when the volume of water to be treated is large, Jan is of

1 It is recommended to use a piston concealment strategy to prevent JIS water from being subjected to the deflections imposed by the side streams (A and 8'). See provisional sequence in Figures © to 01. For the use of small equipment and/or low cost installations it is preferable to provide a solution requiring cexternally attached double pistons as shown Shown according to the sequence

os provisional in Figures 11 through VE which are not described in detail in this Tokai statement because these forms would be self-explanatory to the subject matter expert.

A particularly interesting alternative is to not use a plunger.”

dic will be replaced by the division plane only between water masses; As well as the use of specific process conditions rather than physical elements, such as the need for a flow rate

laminar flow Jada tv. and assuming certain limitations; Jie The degree of mixing given in the separator plane. This is for the benefit of achieving a less complex design and a higher speed

higher fluid speed may be required in systems with a high degree of reliability in places where

Specialized labor is available for maintenance tasks, and where it is desired to reduce labor costs

Compartment size extra. Such a system is shown in Figures 11 through OA, where

ve show from these figures that the mother chambers are toric (with terminations as

ARR

Vo

In the system (Bae SA) they may be fitted with straight and curved lengths to facilitate the achievement of Cus non-turbulent flow special flow meters (1 YY) flow meters are used. Lage (FY on piston and associated detection fixtures supplied up to oY) Cycle changes are set 5 times in the main chambers.To avoid offsetting time in the AES separating plane water due to Cycle changes; flowmeters (VY, 17, and 7) are synchronous; Although Gy is the preferred embodiment, the position of the piston in the separation plane can also be determined by means of sensors da gla below the conductivity sensors. Etc., with adequate distribution in appropriate places; or simply by using the proposed patent Ve timer device; The valves are able to close very quickly; The more the Gay valve and the sequence of subsequent operations for all valves JS operation time, the shorter the operation time, the better; Where the maximum benefit is achieved from the speed of the fluid and its kinetic energy; to zero. 1 Auxiliary pump No. stopping time and additionally; chamber-filling pump downtime and this inactive period or chamber-filling pump downtime may be reached yo in the operational sequence; As explained above intermediate state as a result of the intermediate state No. 1 in detail; By returning to a stage in which each of the two chambers is under high pressure during supply

their contents to the membrane. An additional important feature derived from this subject is that the valves may be chained © by means of a cam or simply by forming them into a single de sane; As in multi-way valves, because de yu valve operation 1 may be as fast as necessary; As in the case of an internal combustion engine, and in Als compartments ld high operating speed; Tests on a prototype show that their sizes can be substantially reduced by more than ve 100-fold; In particular in the case of the piston-free chambers shown

v1

In Figures 117 OT Ve and OA the volume increase derived from the resiliency of the chamber walls when compressed by the high-pressure pump (1) is less than 100 times; The pressure of the pump and the diaphragm is practically imperceptible. This means that the previous pressure valves, Toki (15), may be canceled because there is no need for 1 distraction, and thus JI, the number of valves installed is significantly reduced. As shown in figures 01 odd and YY Valve No. 9 is now integrated from the outside with the rest of the valves, which simplifies both the design and installation of the valve and the integration of the valves into a single-body multiple valve. Diameter diameters are low; it is more effective if the water rotation time in the kinetic cycle water rotation time ve is short; because of the load loss in small-diameter tubes. Greater than Gag losses for Figures 117 15 Vo and 81 and the water requires a shorter shutdown time; however, if the valve change velocity is large, as intended, the system is YG due to prevention of Taig ram impacts Next with water or brackish water

in motion; non stop; And with the benefit of its kinetic energy; As previously explained. vo. Figure YY shows schematically the continuous kinetic cycle system embodied, Ga, for the best achieved improvements; Including the rest of the elements of the desalinating plant elements da sal. Since this process has been described by Gig for Figures 1 to VY, the following description is directed towards the structural and functional differences I introduced New improvements. As shown in Figures 1 to 11, a (Y + V) auxiliary low pressure pump supplies raw water yall 5 (the “Y +1”) An auxiliary conduct internal circulation pump (011) handles the same amount of water as the auxiliary pump (Y+1) and the same amount of brine water is discarded. The internal circulation pump (YF) performs Its function in a closed circuit with a small differential pressure is Gila for the vo load loss of brackish water in the membrane; although the housing of the pump is "tumor exposed to pressure".

The high pressure (YY) pump that handles the water flow generated at permeation ye pressure does not work. The internal circulation pump (¥ 0) takes water from the (Y YY) high pressurized conductor and after it passes through the membrane; It comes out in the form of brine water that enters the return conduct (YY €) return conduct at high pressure 0 as well. Finally, it should be mentioned that the discharge stream (YY) leaves the circuit and brine water comes out of the auxiliary pump (0110) at a low pressure from a practical point of view. It should be realized that the raw water to be desalinated or only brine water circulates in each of the two main compartments ('Y 10) (Y 0) and the two valves (1) (TY) as the resulting desalted water is fed to the outside via the -(Y + £) osmosis membrane.\ After describing the aspects of the system in what Relating to inverse osmosis in front The continuous kinetic cycle system is described in this statement below according to an embodiment using two Cus three-way valves The fase does not change the use of kinetic energy but nevertheless provides a new view of the various elements used; see Figure YY Figure YY shows an inlet valve (1) and an outlet valve (1) (vo) each coupled with AY mechanically coupled through a bridge bridge (8). The entry valve (VV) comprises an entry slide (©V) with a single groove (AY) that slides axially into the inlet cylinder (0) forming a space annular space Lila in combination with entry housing 0 ( 8: ) inlet housing and divides this entry space into manifold 5 (v v) first manifold J, manifold (YA) central manifold Jaw sie and third manifold (v 9 ) third manifold Y. by means of a first annular separator J ol (¥ °) and a second annular separator (of ) second annular separator representing the entry cylinder (de gana (oY) first of the entry ports for brine water 711) first brine entry ports ( and a set of pressurizing ports (V£), provided that the latter is placed near the first annular spacer (57). Thus, the first entry manifold (VV) is connected to the inner cavity internal cavity in the inlet cylinder re (27).

Ya

placed on (AV) via the set of ports of the middle inlet manifold (OF) the entry thus described (TY) and the inlet valve middle plane is an extension of its middle plane and thus the clongitudinal axis with respect to the plane This medium is perpendicular to its longitudinal axis Sila with the inner cavity of the inlet cylinder (0) through (VA) the second inlet manifold (VE) and the previous pressure ports LES (711) are connected to the second set of brine water inlet ports 0

Lian equivalent. It should be understood that connection between the different manifolds may or may not be possible (91). Sliding entry slide (AY) Depending on the position of the entry annular notch and with respect to the outlet valve (11'); it is formed in a manner similar to that of forming Valves (85) (45) represent two annular grooves (P00) except that the exit slide (VY) enters the entry instead of one, as in the case of the entry slide (01). Accordingly, it is possible - © ('797) Connection between the inner bore of the outlet cylinder (7©'); the first outlet manifold where they all form sizes (VA), the second outlet manifold (VA) and the middle outlet manifold outlet housing included between exit cylinder (5*7'); annular volumes annular exit housing and second exit annular spacer (08) through (oF) first exit annular spacer (501''); Brine water discharge ports de gene AND holes 1 of Tax correspond and are close (VY) to first exit manifold (TOY) in exit cylinder (YVY) (71") and coincide A set of brine discharge ports (OF) first annular outlet separator placed equidistant oY) with the second outlet manifold (POY) in the outlet cylinder (NY) relative to the middle plane perpendicular to the longitudinal axis of the outlet valve symmetrically and finally; A set of ports in the middle outlet manifold (87') connects to the © outlet cylinder with the middle outlet manifold (78'). And the internal cavities show their internal cavities (TOY) on each former ('76) (VT) small depressurizing ports Mla two sets of (TAY) one side of the aforementioned exit manifold ports Other than single direction flow valves, one-way flow valves (YAY YY) are known in the previous patent.

1 and closes at a higher pressure in the direction (‘700) receiving raw water from the auxiliary stream and 716”; it has the same properties as the previous valves; 706) the opposite; and the non-return valves open - (Y YY) pressurized conduct To allow the passage of water towards a pressurized stream, the occurrence of (' +1 and 8) circulation valves, and finally, the main circulation valves allow, when all Ja is closed and only open, a "continuous kinetic cycle" effect 0 The entrances and exits of the main chambers relative to the outside, and the water circulates inside the chambers in the form or kinetic energy, and in each cycle, inertia thanks to the inertia closed ring sd, specifically the movement of opening and closing of the main valves with three passages; Four continuous motions are produced, two for each main compartment (two for brackish water and two for desalinated water). When the two sliding slides are YT, this effect is realized in the case represented in the figure, with no water entering or exiting From the chamber (Lila in the position shown) '51 and accordingly it is necessary to open the first main circulation valve (Yeo) the passage of water from one side to the other TE thanks to the energy stored in his movement. Figure 701 shows an intermediate space (from right to left in the drawing) and its rotation through an intermediate space vo and the entry and exit housings (00) (100) that (oY) (oF) between the entry and exit cylinders The formation of the external valve body subject of research is epicycloid. Figures (77) 5 (£0) show a preferred embodiment of the over-the-top circular drive mechanism (00) using a connecting bridge (1) (VY) for each of the two sliding valves driving mechanism Provided with (4+) driving rod The bridge has a hole in its central part through which a drive rod passes © with two butt ends (11) 5 (141) designed to push the bridge (00) along both directions. It rotates around a medium wheel (37) Planetary gear The drive rod is in turn by means of a Colby gear ( ay ) connecting rod Driven by means of a connecting rod (4 ) central wheel placed at entry points (('YYO) ((YY0) and between Relates to thin plates in the flow turbulence resulting from absorbing for the purpose of absorbing (0 0) (Yeo) the two main compartments vo

The passage of JS raw water or brackish water through the inlet and outlet valves (11) (1) and its shape may change according to the volume of the selected water de jug unit, etc. However, it is usually designed based on a laminar network. sheet lattice (40) and concentric tubes (31) with radial sheets (97) or a set of parallel tubes (3A) See figures from SEY AY and description begins in Figure (Yo). wherein the inlet and outlet slides (01) (70) are at their stroke (lower position). At this Ala yall opens the feed water JAI through an auxiliary stream ('710) the non-return valve (1?) while the end of the other main chamber (01©5) is free to connect with the outside through the discharge chute (771). It passes through the inlet valve (TY) and the outlet valve (16); it runs freely; it exits through the discharge channel (771) and thus the brine water that occupies at this moment the first main compartment (011) is thrown out. The second main (706') is fully active and the Cua supplies its 1s with raw water through a pressurized stream (777) and then to the membrane (£ oY) and receives brine water through a return stream (YE) The location of the sliding slats (51) (51) allows free passage of water, which fills the second main compartment (706'); keep; Because of its high pressure, the non-return valve (VIF) is in the closed position. The Lilie (Y1£) non-return valve remains

da is for the lower pressure in the first main chamber relative to the pressurized duct (77?).

x. In Figure YT the slide valve slides advance to a point where the exit slide slide (P01) closes the exit manifold (AY) ports while the exit valve (11) closes the GIS because the common passage; Specifically, the central one; it is closed. At this point, the first main chamber (510), which is filled with raw water from the sea, does not receive any water supply from the auxiliary stream (0170'); thus the non-return valve (7011) closes despite its internal pressure

auxiliary feeding conduct Low; which is approximately equal to the auxiliary feed pressure Yo

(Y +0) At this point; The water that circulates inside the first main chamber (”701) thus finds no exit path for the force of its continuous movement, thus opening the discharge channel (Lillie (171) to allow the passage of water from the manifold (01) first recirculation valve). First recirculate and re-enters into the main chamber (VY) to the first inlet (YY) manifold first exit thus regulating the motor cycle step o (YY0) through thin sheets in the flow (Yeo) At this stage, all the remaining brine water is thrown into the first main compartment (0 5) where it remained as shown in the figure oY 00 (and no change occurred in the main chamber through the force) 7016) All the raw water towards the membrane Go and the brine water pushes the pressurized WYO (177) © The slides in both valves advance slightly as well and the YY and in the figure to accomplish the (VE) operation determine their position Now for the next step where the small outlets of the previous pressure are opened and the high pressure is passed in the return stream (;?) to the “prior pressurizing” of the previous pressure

Cla gb This previous compression process is carried out through (7005) the first main chamber and solves two problems. It includes a small coil shock absorber, as in an 8 transfer of oil mass due to fluid transfer (014). Pressure in the membrane Descent The first problem is simple subsidence due to rebound expansion from one chamber to the other as a result of expansion 0 Low-pressure chambers and ducts that suddenly become compressed; the effect is the “sudden previous” in the sudden ways The second undesired baal which is resolved by a process which is required to close this valve is ela sida of the first recirculation valve (0900); which is beating© at this point. which remains as shown in (TY). 0) and no change occurred for the second main compartment

Figures YU and Yo indicate that the sliding slides advanced slightly as well and reached the point YA. The figure shows (AY) in its stroke, while the middle entry manifold outlets are Lila middle point xo

ARK

YY

This means chalf-open Aa side half (711) ((YVY) and the first and second exit manifold ports (77) feeding the pressurized duct (706) ¢(Y +0)'706) that the flow from the two chambers The two main changes are made to continue equal dua for each compartment.This point is considered the turning point of JS Te sa and supplies all (Trg) pressurized stream (777) in the uninterrupted supply of water to the membrane

AYYT) From the two main chambers containing raw water to the aforementioned pressure stream 0 a, the sliding slides continue in their path. The sliding inlet slide (YA and in fig. VA) closes the brine and pre-pressure ports (117); (74') in the second inlet manifold (0) without contact with the outside while it continues (TY 0) Which leads to leaving the second main compartment, and the water content is YA. The work is as shown in Figure (015) The first main compartment is movement at this stage; it works as it is Alla brine in the second main compartment (700) In - that is, it begins to rotate in a loop (Yeo) with respect to the first main chamber (YU) shown in Figure (Y +9) as a result of the inertia of the brine water mass that opens the second recirculation pump (loop below ) 7016( (which is considered to be the main component of the invention). The second main chamber is still pressure. The slides advance slightly as well while the chamber operates oF and in vo as shown in Figure 79; although when The first main (Y 00) pressure reducing outlets open, the high water pressure in the second main compartment (0 + 7 ') drops to the previous pressure (V1) and thus enables (YY) atmospheric once the brine water exits to Sea by way of the discharge stream from (711) from opening the non-return valve (‘700) low pressure in the auxiliary stream and VT through a very small outlet in the previous pressure reduction outlets is not considered ©

YY Pre-pressure This is as important as the "pre-pressure" process described in the figure, whereby the water flows out under pressure in a small amount equal to the amount that the main chambers are able to store due to their expansion under the high pressure; However, the resulting minor noise can be eliminated.

ARK

YY

With the slide valve semi-cycle specifying the end of the half-cycle of the sliding valve 1. The figure in (Y 10) shows the position of both valves at the end of their stroke, while the first main chamber continues and the second main chamber continues (705' ) Discharging the water 700 Work as shown in the figure by means of the discharge chute (177); The raw water enters through the evacuate brine channel (717) and the brine discharge ports (YY) where the auxiliary non-return valve (YY) is 0 while the contents of the main chamber exit GIS open (AY ) and intermediate outlet manifold ports (771) by means of the Las discharge chute as described (TY 10). The second slides are now at the end of their stroke; ) with raw water and solutions of brine water that enters by force into the place of raw water in the first main chamber (©107); it reverses the (YYE) return direction - and the cycle repeats itself as previously described in this statement. 1108 valve stroke The stroke of the slide valve, and the figures from 76 to 0 show the mechanical overhead cycloidal process related to the phases

FY Differential continuous motion desalting unit process. And so the two forms correspond to +? And in a stage (701©) with the first main chamber Yo being the same valve location shown in the figure and the second main chamber (0 + “) supplying raw water filling stage raw water filling stage ve Via the compressed channel (777).The (Vf) for the pressurized JA penetration into the membrane is considered a period of inactivity TY and VT The elapsed time between the positions of the planetary gear (17) shown in the two figures No movement appears of the bridge (00) allowing the first main compartment Cua dead time to be filled with raw water and supplying the total amount of raw water contained in the second main compartment (001)

AY 8) through the pressurized channel (777) towards the membrane (01 *) © and shows the positions of VE) the moment at which the ports of the previous pressure open YA and the figure shows in its cycle (‘7006) while The first main compartment 717 is the numerous valves in the figure supplying it with pressurized raw water. (‘706) continuous movement and ends the second main chamber. Figure 4 shows? the second Fe (17'); with the valves positioned as shown in Fig. vo

The brine in the second main chamber (0 + VY) is in its continuous motor cycle, while the first main chamber (00 Y) begins the step of supplying it with pressurized raw water. Finally, Figure 50 shows the end of the half cycle of the planetary gear (47) and a paragraph begins New stagnation during which the total amount of pressurized raw water present in the first main compartment 0 (015) should be supplied and the total filling step of the second main compartment (0+) with raw water should be completed. Figures show YY to Tawa Yo industrially industrial for the purpose of the invention.As noted, the two main chambers (0 + ¢(Y) (517') constitute the inlet and outlet valves (VY) (VY), recirculation valves and non-return valves (09) (C17) YT ) (TY) (YVE) © and (?7) compact assembly that can be moved easily in the installed state. Yas from getting carried away with the installation work; All that is required is the installation of the auxiliary duct (0170'); the compact duct (777)”; Return stream (YE) and discharge stream (YY) and connect pumps.

Claims (1)

Yo protection elements inverse osmosis water desalinating 1-1 pressurized continuous al plant Y “kinetic cycle mother chambers 7 ¢ Wherein pressurized continuous kinetic cycle mother chambers°° comprise a first mother chamber 1 and a second mother chamber that is alternatively pressurized; While unit 7 inverse osmosis water desalinating plant A additionally includes: 9 high pressure pump installed in parallel with internal circulation pump 01; 1 where the first mother chambers form a closed circuit Olsey; 1 where the second mother chambers form a closed circuit; Cus VY the first closed circuit is separated from the second closed circuit Ve; During the operation of the inverse osmosis water desalinating plant Vo, the water is able to circulate daha in each mother chamber V1 at all times in one direction and in a continuous pattern. =Y 1 unit for desalination of water with reverse osmosis, Gi inverse osmosis for protection element 1 7 where a sequential function multiple valve is provided with six v ways: =F 1 Gi inverse osmosis water desalination unit for the protection element oY Y where it forms the aforementioned multiple valve via a cylinder A! v empty cylinder with corresponding 5 exit holes £ internally sliding piston with circular grooves and Cua means of imperviousness multiple valve includes 1 grooves and six -outlets inverse osmosis water desalinating unit 4-1 The first is the shape of the mother chamber Cua 0 according to the protective element plant Y or any helicoidal “zigzag” shape zigzag oval annular 1m oval shape 7 storoidal shape the second another mother chambers shape; And the mother's compartment has a shape. Al shape or any chelicoidal shape zigzag 218228 spiral oval 0 inverse osmosis water desalinating © 1 - The first on the mother chamber The mother chamber includes Cua oY of the protective element Gy plant Y First party and second party; Where the first party is connected to the second party to form a closed circuit 1 tclosed circuit ¢ ° Where the second mother chamber includes a first terminal and a terminal (ld where 1 connects the first terminal to the second terminal to form a closed circuit 7 where the first closed circuit and the second closed circuit A do not share a common chamber portion inverse osmosis water desalinating unit 1-1 first form mother chamber cua 0 for protective element Gy plant 1 and be ¢helicoidal “zigzag zigzag” oval, toroidal, v-shaped, zigzag, oval, toroidal, annular, shape 1 7- Inverse osmosis water desalinating unit Gg plant Y for protection element 0 where each mother chamber ol includes a means and means of separation between masses of water csalinity Each means of separation includes a piston “0:” that has an apparent density ° similar to the density of water. ——A 1 inverse osmosis water desalinating plant 7 according to protection element “Y” where each piston receives a corresponding rotary and corresponding rotating basket equipped with a non-return valve -non-return valve 1 4- inverse osmosis water desalinating plant Gy Y for protection element A, where each piston with the basket achieves the corresponding position v bypass position for -concealment strategy -01 1 inverse osmosis water desalinating Gi plant Y for protection squeeze 5; Where each mother chambers includes a means of separation v means of separation between masses JIS water of different salinity and each ¢ means of separation includes two pistons Lg I pistons bulk density apparent density ° similar to the density of water and can be fixed by means of clamps 1 narrowing the section of the tube tube inside which the pistons rotate -11 1 reverse osmosis desalination unit inverse osmosis water desalinating plant according to the element of protection 0 Cua the two mother chambers do not include 7 physical means to separate water masses of different salinity ¢ and achieve separation separation The aforementioned is through controls for the water flow Ya adjustments ° make the water circulating flow inside the mother chambers 1 the first and the second laminar as much as possible and prevent access to the turbulent flow 7 condition and provide flow meters In unit plant A to run the cycle in the mother chambers according to the supplied flows q or by measurements of salinity or conductivity of water. inverse osmosis water desalinating unit -1" 1 includes: Cua VY according to protection factor plant Y 3 Inlet valve formed by means of an inlet slide 481 Jia shaped in the form of a solid cylinder with an annular groove sliding horizontally into an inlet cylinder formed together with a housing inlet housing annular space 1 divided into a first inlet manifold » middle manifold 7; a second inlet manifold via a first annular inlet separator A and a second annular inlet separator; The entry cylinder “port Mis inlet cylinder 49” represents the first of the middle inlet manifold and the previous pressure port “prior pressurizing port 01” the first corresponding to the first inlet manifold »port of the middle inlet manifold 11 corresponding to the manifold Intermediate inlet manifold, the Sa VY port of the intermediate inlet manifold, and a second prior pressurizing port Vr corresponding to the second inlet manifold. ¢ \ outlet valve formed by means of an outlet slide 48) jie formed in Vo form a solid cylinder with annular grooves formed together with an outlet housing annular space Lila 13s outlet housing divided into inlet manifold 7 first; middle outlet manifold; And a second outlet manifold VA through a J of annular outlet separator and a second V4 annular outlet separator, and the outlet cylinder represents an outlet Yq of the first port manifold and outlet manifold The first view of the outlet manifold Exit Y. Middle outlet manifold The middle view of the outlet manifold Exit 711: This is the second; second manifold Views of the outlet port and YY exit port to the inlet valve tightly connecting the inlet valve driving bridge YY mother chamber connecting the first end to the mother chamber Cua Soutlet valve Yi mother chamber The second end of the mother compartment 0 is connected to the first inlet manifold, the first Yo; The first end of the outlet manifold is connected to the second exit manifold 7 and the second end is connected to the second inlet manifold with the mother chamber 77 ¢ outlet manifold of the second with the second exit manifold mother chamber YA It receives the raw water supplied by the auxiliary conductor auxiliary pump and the inlet manifold and directs it to the auxiliary pump re. Special non-return valves, the second through non-return valves, inlet manifold 791, the first, outlet manifold, connected to the outlet manifold, pressurized conduction, YY, non-return valves, the second, through the outlet manifold. private rv exit manifold; The raw water from which desalination should be desalinated is directed to the non-return valves ve ¢inverse osmosis membrane vo starting from the return conduct a return stream 74 thrown to the inlet manifold brine and directs the brine water inverse osmosis membrane rv ¢inlet valve inlet manifold YA outlet manifold unloading conductor va 'outlet valve non- return recirculation valve 3 inlet manifold 1st to outlet manifold from exit manifold 7 2nd non-return recirculation valve non-return recirculation valve Second inlet manifold to outlet manifold from exit manifold 2 M-1 “01 inverse osmosis water desalinating plant Y according to the protection element OY, where Ba is the outlet cylinder, two series of two prior pressurizing ports so that they are on each side of the port ¢ of the intermediate outlet manifold. —V Ey inverse osmosis water desalinating Gig plant Y of protection element 01 where the said driving bridge 7 is operated by means of a variable sequence that produces stops It stops at extreme points of its stroke and slows down at intermediate points corresponding to the opening of the prior pressing ports ° I and II. —V0 0 inverse osmosis water desalinating unit Gi plant Y of protection element 04 where the operation of the said driving bridge 7 is accomplished by means of an epicycloid mechanism comprising Toothed wheel ¢ fixed central dented wheel around which a planetary gear rotates and on its circumference effectively connects the end of a connecting rod and drive connecting rod drives 1 drive rod equipped with two butt ends designed To withdraw the driving bridge 7 connected to the inlet valve and the -outlet valve z 3 All -11 1 inverse osmosis water desalinating Y 6 according to the protection element VY, where two thin plates are placed in the flow laminator v at the inlet of the first and second mother chambers for the purpose of absorbing the turbulence resulting from the passage of raw water or brine. ° Through the inlet valve and the -outlet valve A inverse osmosis water desalinating unit for the removal of salinity from water by reverse osmosis 1-17 of protection element 07 where the two thin plates in the flow, Gi plant .sheet lattice, are formed using a lattice flow laminator and inverse osmosis water desalinating Reverse osmosis water desalination unit —VA 1 flow laminator Where laminates are formed in the flow V1 of protection element GE plant Y radial sheets with concentric tubes using several concentric tubes 1 inverse osmosis water desalinating Reverse osmosis water desalination unit -14 0 flow laminator, where laminate sheets are formed in the flow 0 of the protection element Gd plant Y .parallel tubes using several parallel inverse osmosis water desalinating units Reverse function - 701 1 sequential Cusco is provided for the element of protection Gig plant Y ways with six lanes function multiple valve 7 inverse osmosis water desalinating unit -71 01 mentioned above multiple valve where the multiple valve forms 700 for the protection element Eg plant Y corresponding corresponding exit holes Cd empty cylinder empty cylinder way v with circular grooves 293 internally sliding piston and sliding piston outlets ¢ includes Cua means of imperviousness Circular grooves ° -outlets Six exit holes Two grooves Multiple valve 1 inverse osmosis water desalinating unit —~YY 1 pressurized Equipped With main pressurized compartments with continuous kinetic cycle plant Y Cua continuous kinetic cycle mother chambers ¥ The pressurized continuous kinetic cycle mother chambers ° include a first mother chamber and a second mother chamber 1 alternately pressing talternatively pressurized where v the inverse osmosis water desalinating plant A also includes: 9 high pressure pump installed in parallel to an internal circulation pump 11 01 where the first mother chamber forms a first closed Scircuit VY while the chamber forms The second mother chamber is a second closed circuit VY where; During the work of the Ve osmosis water desalinating plant 176:56, the water is able to circulate Veo inside each main mother chamber at all times in the same direction V1 in a continuous manner. fcontinuous fashion and VV where each main mother chamber includes a means of separation means of VA 00 between Cua different salinity water masses Va includes each means of separation means of separation on a sphere-shaped 3 —S piston Y. with an apparent density similar to that of water. inverse osmosis water desalinating unit -77 1 in corresponding rotary piston where each piston receives (YY of protection element GG, plant Y -non-return valve equipped with check valve) corresponding rotating basket and inverse osmosis water desalinating unit -74 1 Gig plant Y of protection Cua YY scores each piston with corresponding basket and corresponding basket bypass position in response to ¢-concealment strategy =Yo 0 inverse osmosis water desalinating plant Y equipped with pressurized main chambers with continuous kinetic cycle pressurized Cus “continuous kinetic cycle mother chambers v” The pressurized continuous kinetic cycle mother chambers ° includes a first mother chamber and a second mother chamber 5 Cua talternatively pressurized The inverse osmosis water desalinating plant A 7 also includes: A high pressure pump installed in parallel to an internal circulation pump 'internal circulation pump ye. 11 where the first mother chamber forms a first closed circuit VY and the second mother chamber forms a second closed circuit VY ¢ second closed circuit where; During the operation of the Ve water desalination unit with reverse osmosis in the cinverse osmosis water desalinating plant, the water is able to circulate the Vo Jala circulate in each main chamber, the mother chamber, the chambers at all times 1 in the same direction and in a continuous manner. ¢continuous fashion and Cua VY Each main mother chambers includes a means of separation VA between “different salinity water masses V4” where each means of separation includes means of separation On two pistons in the form of a sphere-shaped piston Y. With an apparent density similar to that of water, 71 is liable to be blocked by clamps narrowing the section of the tube in which the pistons YY rotate. ve inverse osmosis water desalinating unit -71 0 pressurized plant Y where the pressurized continuous kinetic cycle mother chambers include 1 pressurized continuous kinetic cycle mother chambers With a continuous kinetic cycle ¢ second mother and a second main chamber the first mother chamber on the first main chamber ° includes Cua talternatively pressurized removal unit chamber 1 also inverse osmosis water desalinating plant salinity of reverse osmosis water 77 on: A mounted in parallel to an internal circulation pump high pressure pump q tinternal circulation pump 1 closed circuit Olsey 558 mother chamber forming the first main chamber Cua 11 circuit second mother chamber while forming the second mother chamber ¢first closed circuit VY where; During the operation of the water desalination unit ¢second closed circuit VY the water is able to cinverse osmosis water desalinating plant in reverse osmosis Ve chambers at all times mother chamber inside each main chamber circulate Veo and continuous fashion 1 first and second mother chambers Cua Vv between brackish water physical means of separation does not include a physical means of separation VA The aforementioned separation is achieved by means of controls for the flow of water © different salinity water masses 14 inside the two main chambers, water circulating that makes the flow adjustments Y. as much as possible and prevents laminar first and second mother chambers. 1 In that cycle, the turbulent condition is to reach the state of turbulent flow, YY, according to the flow meters supplied, operating by means of measuring devices for the flow, YY, or the water conductivity, or by measurements of the salinity supplied flows. Ye .conductivity measurements a vo inverse osmosis water desalinating unit -77 01 desalinating plant P71; Where peated Gig plant Y desalination unit includes: Lal and t An inlet valve formed by means of an inlet slide formed into a solid cylinder with an annular groove 315% horizontally slides axially 1 inside an inlet cylinder Combined with Sie 7, they form an annular space Gila fa cinlet housing divided into a first inlet manifold A, a central manifold, and a second inlet manifold q via an entry separator. first annular inlet separator (Ve) and an annular entry separator (5) second annular inlet separator. The Js—aal inlet cylinder represents 1 first central inlet manifold port and VY port. Prior pressurizing port Js 8 views of the first inlet manifold 7 and a port of the central inlet manifold port Ve views of the central inlet manifolds and a second port of the second central inlet manifold port Vo and a second prior pressing port Vi corresponding to the second inlet manifold ¢ second inlet manifold 7 outlet valve formed by means of a sliding outlet slide VA formed in the form of a solid cylinder with cannular grooves 1 combined with a cutlet housing forming a space annular space Gila divided into first inlet manifold 7, central outlet manifold 7 and second outlet manifold via first annular outlet separator YY and exit separator A second annular ¢ second annular outlet separator YY and the exit cylinder Mia outlet cylinder represents the exit of the first outlet port J sl corresponding to the manifold of the first outlet manifold Y and a port for the middle outlet manifold central outlet cmanifold port ve Mia y central outlet manifold views of the exit 71 second outlet port corresponding to the second outlet manifold ¢ second outlet manifold 7 driving bridge securely connecting the inlet valve to the outlet valve YA 706E; Cua The first mother chamber includes a 79 first end connected to the first inlet manifold and a second end rv. It is connected to the first outlet manifold ¢ first outlet manifold and where the main chamber 791 second mother chamber includes a first end connected to the second inlet manifold vy and a second end Connected to the second outlet manifold TY ve is a cauxiliary conductor that receives the raw water supplied by the auxiliary vo pump and directs it to the first inlet manifold v1 the second inlet manifold by means of special non-return valves vv; YA pressurized conductor connected to the first outlet manifold ra and the second outlet manifold by means of 6 special second non-return valves; The raw water 1 from which desalinated is to be removed is directed to the 'inverse osmosis membrane ey 8' a return conductor that starts from the inverse osmosis membrane tt and directs the rejected brine water brine to manifold to central inlet manifold at tinlet valve unloading conductor coupled to central outlet manifold 7 at outlet valve 3 recirculation valve first first non-return recirculation valve allowing £4 passage from the first outlet manifold to the first inlet manifold 8 and Manufacture 2 second non-return recirculation valve ov allowing passage from the second outlet manifold to the oy -second inlet manifold —YA removal unit Salinity of inverse osmosis water desalinating Y 4 according to the element of protection (YY) where the outlet cylinder represents two series of prior pressurizing ports ctwo series of prior pressing ports so that they are on each side of Both sides of the central outlet manifold port 1 4 ?- inverse osmosis water desalinating ell unit for protection element (YY) where the operation of driving bridge wall is mentioned by v by means of a variable sequence producing stops at extreme points of ¢ its stroke and slowing-down at intermediate points corresponding to the opening ° of the first and second preceding pressure outlets “first and second prior pressurizing prots = e 1 inverse osmosis water desalinating Gg plant Y of Cua (YS) protectant operation of driving bridge mall is accomplished by means of a cyclic structure Overhead Jaks epicycloid mechanism on a fixed central dented wheel ¢ around which a planetary gear rotates and on its circumference a periphery ° effectively connects the end of a connecting rod and drive connecting rod drives 1 drive rod rod equipped with two butt ends designed to draw the operating bridge 77 operating driving bridge which is connected to the inlet valve and the outlet valve A - 1 “1” reverse osmosis water desalination unit inverse osmosis water desalinating YA flow laminator, where two thin plates are placed in the flow, YY, of the protective element, Gg plant Y first and second mother chambers, at the entrances to the first and second main chambers 1, or raw water resulting from the passage of raw water, absorbing turbulence, to absorb turbulence -outlet valve inlet valve through inlet valves brine inverse osmosis water desalinating reverse osmosis water desalinating unit —TY 1 where the two thin plates form in the flow (oF) according to the element of protection plant 7 .sheet lattice flow laminator v inverse osmosis water desalinating YF 0 —2 thin sheets in flow forming FY of protector Gi plant Y with diagonal plates concentric tubes sae using flow laminator 3 radial sheets ¢ inverse osmosis water desalinating unit —YE 0 where the two thin plates form in flow FY according to claim 4 Y .parallel tubes using several parallel flow laminators