CN100404112C - Fitting for installations having pressure exchangers - Google Patents

Fitting for installations having pressure exchangers Download PDF

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Publication number
CN100404112C
CN100404112C CNB2004800064417A CN200480006441A CN100404112C CN 100404112 C CN100404112 C CN 100404112C CN B2004800064417 A CNB2004800064417 A CN B2004800064417A CN 200480006441 A CN200480006441 A CN 200480006441A CN 100404112 C CN100404112 C CN 100404112C
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China
Prior art keywords
annex
control assembly
shell
pressure
opening
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CNB2004800064417A
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CN1758951A (en
Inventor
S·鲍姆加滕
S·布罗斯
B·布雷赫特
U·布鲁恩斯
S·弗拉克
C·耶格
W·科哈诺夫斯基
W·克内布尔
M·埃勒加德
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KSB AG
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KSB AG
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K11/00Multiple-way valves, e.g. mixing valves; Pipe fittings incorporating such valves
    • F16K11/02Multiple-way valves, e.g. mixing valves; Pipe fittings incorporating such valves with all movable sealing faces moving as one unit
    • F16K11/08Multiple-way valves, e.g. mixing valves; Pipe fittings incorporating such valves with all movable sealing faces moving as one unit comprising only taps or cocks
    • F16K11/085Multiple-way valves, e.g. mixing valves; Pipe fittings incorporating such valves with all movable sealing faces moving as one unit comprising only taps or cocks with cylindrical plug
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/06Energy recovery
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/10Accessories; Auxiliary operations

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Nanotechnology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention relates to a fitting for switching over fluid paths, particularly for installations having pressure exchangers with tubular chambers (3), which are alternately flown through, whereby a rotating control element (10, 10.1) having a number of flow paths is mounted inside a housing (11). The housing (11) comprises a number of connections (12, 16, 17, 46) for connection lines, and is connected to a first pipe system and to an end of at least one pressure exchanger. Another end of a pressure exchanger is connected to a second pipe system with the interconnection of other fittings. The control element (10, 10.1) is provided with a motor-operated drive shaft (50), and the flow paths of the control element (10, 10.1) are alternately connected to openings inside the housing (11). A flowing to the control element (10, 10.1) ensues from an axial and/or radial direction, and a flowing way from the control element ensues in an axial direction.

Description

The annex of band pressure exchanger equipment
The present invention relates to a kind of annex, especially the annex that has the pressure exchanger equipment of the tube chamber that alternating current crosses, wherein be furnished with in the enclosure one have a plurality of flow channels can rotating control assembly, shell has the interface of a plurality of connecting lines, shell and one first pipe-line system, and be connected with at least one tube chamber end face separately, wherein tube chamber another end face separately is connected with one second pipe-line system under the switching of other annex, control assembly is equipped with a motor-driven power transmission shaft, and the flow channel of control assembly alternately is connected with the opening of arranging in shell.
This pressure exchanger is made up of two or more tube chambers, and annex is equipped with in its end.Open and close accordingly by annex, tube chamber alternately loads with the liquid that contains different-energy.Therefore in tube chamber, in equipment or in equipment operation process, a kind of high pressure of liquid can pass to another liquid that only has slight pressure.Therefore can save cost of energy in the equipment by means of this pressure exchanger, and booster pump can do littler.
Reverse osmosis is through being usually used in the processing of water.By a film system, when fluid flow was big, the film system will be made up of a large amount of membrane modules liquid stream wherein to be purified with high-pressure extrusion.Because always have only the part of liquid to be purified can flow through diaphragm, so in this membrane module, can realize separating of pure water and the concentrate that gathers by diaphragm.The part that flows through perhaps also can be used as the penetrant at the diaphragm opposite side as pure water, as utilizing part to flow out.The part that does not flow through is as saline solution, and a kind of liquid concentrate that is gathered by salt and mineral matter leaves membrane module as part unavailable and that be under the high pressure.Under the membrane module inlet pressure of about 65 crust, this pressure is probably at 2 crust.
By US5306428 reverse osmosis equipment has been well-known, wherein reclaims the pressure exchanger that has used under the tube chamber form for energy.By means of its help, be delivered on the liquid of still preparing purifying by the also higher pressure of the saline solution that flows out in the membrane module, be rich in energy.Therefore in order to produce for the essential high pressure of reverse osmosis, the degree along with pressure improves only needs a small pump driving power for the liquid of supplying with.
Except other annex, annex that has a rotating control assembly is used to control and/or change and enters and from the fluid passage of the saline solution of pressure exchanger.By means of its help, realize using the saline solution of discharging, to alternately loading of pressure exchanger tube chamber by membrane module.Rotating control assembly is a cylinder, wherein according to the arranged in form interface channel of a three-way cock.In transfer process, realize thoroughly closing of all fluid passages.Compression shock for fear of in this class transfer process is furnished with pressure equalisation passage in cylinder.
In the service life of depending on diaphragm, its separating power descends, and therefore liquid to be purified must correspondingly stay in membrane module the longer time.Owing to this reason, under prior art, influence the conversion time of cylinder by means of a servo motor.Yet this annex only is suitable for little reverse osmosis equipment, because the cross section of flowing through in annex is almost the same big with the cross section of flowing through for the treatment of flow in pipes.In main equipment, and the liquid column that moves therein, and consequent power, produce the physical dimension problem of very big annex.
Task of the present invention is, especially develops a kind of conversion equipment for large-scale reverse osmosis equipment, and by means of its help, the liquid streams a large amount of in simple mode can distribute between the different tube chamber of pressure exchanger by interference-free.In the annex of this class, the solution of this problem is to realize in the enclosure by the inflow to control assembly of axial and/or radial direction, and realizes by the outflow of control assembly along axial direction.When axially flowing into and flowing out, can obtain the minimal structure length of annex.Otherwise though annex is a little long when radial inflow, yet the easier control of the axial displacement that is produced.
Task of the present invention is finished by following annex: the annex that promptly is used for the fluid passage conversion, it is used to have the pressure exchanger equipment that is provided with the tube chamber that alternating current crosses, wherein in a shell, be furnished with one have a plurality of flow channels can rotating control assembly, shell has the interface of a plurality of connecting lines, wherein shell is connected with first pipe-line system, and be connected with at least one pressure exchanger end face separately by interface, wherein pressure exchanger another end face separately is connected with second pipe-line system under the transfer of other annex, control assembly is equipped with a motor-driven power transmission shaft, and the flow channel of control assembly alternately is connected with the interface of arranging on shell, and the position of the switch along with control assembly, the highly pressurised liquid that flows into replaces flows to pressure exchanger, and arrive the interface that flows out low pressure liquid by the low pressure liquid that pressure exchanger flows out, wherein, be furnished with the interface of the highly pressurised liquid of an inflow, interface and at least two the pressure exchanger interfaces that alternately load that flow into low pressure liquid with highly pressurised liquid and low pressure liquid, realize in the enclosure by the inflow of axial and/or radial direction to control assembly, and realize from control assembly in axial direction to the outflow of the low pressure liquid of low pressure liquid interface, and in the control assembly transition period, give with annex and be in of the high pressure loading of effective tube chamber that is connected with inlet opening, on control assembly, compare with the flow openings of corresponding to shell therewith at the control opening of the area arrangements of high pressure chest, have an other opening angle.
A scheme is, control assembly is made the control assembly of a hollow cylinder, and dividing plate is divided into the control assembly of hollow cylinder in the chamber in two different pressures districts.In annex, can form chamber additional, that produce the flow divert for the treatment of exchanging liquid with this.Therefore use the thin wall component of simple, an easier control in transfer process for the original control of annex and sealing function.Here another scheme is, arranges additional reinforcement in the chamber in different pressures district.This reinforcement can be made the reinforcement gusset, perhaps makes the thin-wall part that distributes along flow direction for the pressure area that flows through.Same additional reinforcement also can be made annular element.It can be sector or annular element.It improves the rigidity of hollow cylinder control assembly, when being in different following times of pressure condition, the distortion of resisting parts thus.
The different schemes that is used for the operation of hollow cylinder control assembly is, power transmission shaft adopts with dividing plate can transmit being connected of moment of torsion, baffle arrangement is in the mesozone of hollow cylinder control assembly, the arrangements of components that can transmit moment of torsion is on an end face of hollow cylinder control assembly, and dividing plate is fixedlyed connected with control assembly or dividing plate is fixedlyed connected with shell.What therefore power transmission shaft can be direct or indirect is fixed on the control assembly, and it depends on best processing mode.When the zone line of baffle arrangement, guaranteed the distribution in two pressure chambers at the hollow cylinder control assembly.The dividing plate that meanwhile control assembly is divided into two pressure areas can directly be fixed on the control assembly, perhaps is connected with shell.
This scheme is in high-pressure side inlet opening district for this reason, and dividing plate is fixed on the shell with support bar.Meanwhile seal can be arranged between static dividing plate and the rotating hollow cylinder control assembly inner wall surface.Dividing plate and/or the dividing plate that has a support bar that links to each other with shell also can be made interchangeable parts, and it makes that installation and maintenance work is easier, and fixing dividing plate makes axially moving freely of control assembly be arranged as possibility on shell.
According to another kind of scheme, control assembly is a solid cylinder, and a plurality of flute profile flow channels constitute the different pressures district on its circumferential surface.This manufacturing type has been improved strength characteristics.Another kind of for this reason scheme is that on circumferential surface, the flow channel of same pressure area is obtained the balance of pressure thus mutually in radially relative layout.
The cross section of a flute profile flow channel that links to each other with flow openings has formed the control opening of control assembly in addition, and in a high-pressure side inlet opening zone radially, is arranging a cannelure on the shell and/or on the circumferential surface at control assembly.Obtained thus preferably, additional radially connection possibility.In addition on control assembly, between the end of the flute profile flow channel in different pressures district, be furnished with the ring packing district of sealing, and, be furnished with seal on the control assembly and/or on shell in the zone of seal area.And be implemented in the axial displacement unloading between its end face by a relief passage that is arranged on the control assembly.Therefore additional thrust bearing is unnecessary.
The pressure loading of shell is by constituting fork-shaped and/or step-like on the outer circumference surface of control assembly, and the control flume that is connected with the control opening and optimised.In order to resist the load on the outer enclosure, therefore realize autotelic, as to have a high pressure enclosure pressure loading in the zone of control flume.The subsidiary control flume that passes through has obtained an other flow channel, makes the instantaneous possibility that is connected to become between the tube chamber that connects by means of its help.Therefore a cross section of overflow ducts is instantaneous transferring on the control assembly.
When control flume adopts fork configuration, subcontinuous volume flow and pressure condition in annex, have been kept in the transition period.The arcuate member that is in the original Y-piece is arranged in the plane of radially strengthening gusset.This measure has improved the transmission of the power in annex equally.Similarly also can arrange on the inner peripheral surface of wall in the enclosure that constitute fork-shaped and/or step-like, and the mobile groove that is connected with flow openings.
Another kind of scheme according to the present invention on the outer wall of shell and/or in be furnished with the overflow ducts of a plurality of connection flow openings.Help by means of it realizes the exchange of liquid from the tube chamber to the tube chamber during the working cycles of pressure exchanger, wherein annex ensured each connection tube chamber always from the filling of influent zone, and discharge from the trickle zone.For the coupling in pressure exchanger control time, the flow openings of arranging constitutes the part of an adjustable hollow cylinder outer casing inner wall in the enclosure.This additional hollow cylinder outer casing inner wall is made independent parts, and can reverse layout with respect to shell with the flow openings of arranging inside.Therefore under the situation of needs, can mate with the overlapping time of the control opening of on control assembly, arranging.It carries out may be at run duration or at the annex load facility time according to project organization.
In the outer wall of shell, be furnished with a plurality of inlets in addition.Its feasible manufacturing and processing are easier when cast casing.It by the method known with the form of locking member such as embolism, screw element or similarly parts seal.In the outer wall of shell, be furnished with the reinforcement of a plurality of outsides for the rigidity that improves shell.It can be arranged to around shape or externally shell groove just.Because weight and processing, the shell groove is arranged between the overflow ducts.
The tube chamber of pressure exchanger can instantaneously interconnect by overflow ducts during control assembly moves in addition.Particularly when during as attached flow openings, realizing the conversion of impacting with minimum pressure by another angular area expansion at high-pressure side control opening.Angle between opening is measured like this, so that when the opening of tube chamber 1 is just in time closed, and the mobile end of high-pressure fluid, the opening of tube chamber 2 is just in time opened, and admits high-pressure fluid thus.Guaranteed still to wait liquid to be purified and that be in the tube chamber opposite side always to be under the high pressure thus.
Overflow ducts also can be an outer tube, wherein for easy installation, distributes on the outer circumference surface of shell and arranges a plurality of pipe fitting interfaces.According to another kind of scheme, overflow ducts is the flow channel that is integrated in the shell wall.It has reduced the quantity of sealing station.
Another kind of scheme is, by minimum two mutual radially relative flow openings separately, and the control corresponding opening is implemented in fluid exchange between control assembly and the overflow ducts therewith.The symmetric arrangement of opening and flow channel has obtained the supporting that freely moves radially of control assembly in the enclosure.
For soft commutation, the control opening of hollow cylinder control assembly for example can be slot, polygon or other form.The size of position on control assembly and control opening makes no compression shock flow and is converted into possibility.Closing simultaneously of the tube chamber control opening of a connection links with another opening mutually of opening of control of other tube chamber of closing previously, and vice-versa.Because the control opening that enlarges,, realized overlapping with the flow openings of the overflow ducts of fixed and arranged on shell perhaps exactly by its position on control assembly.Meanwhile this overlapping state to commutation and the flow fluid scapus that is influenced thus produces advantageously effect.
At the run duration of annex, on the circumference of control assembly, in graded area, exist different pressure states.Move easilier for the conversion that makes control assembly, control assembly can be provided with a plurality of relief passages on excircle.The zone of determining with this slidingsurface can load with the back-pressure of determining.This class relief passage also can be arranged on the outer wall surface of control assembly, and/or is arranged on the annex case surface that is in face-to-face position.According to its shape and structure, in relief passage, can realize continuous or flowing through of replacing.
When control assembly is bearing on the tortuous case surface of moving towards pivotally, perhaps when the outer casing inner wall as separate part is bearing on the tortuous case surface of moving towards, can obtain a kind of favourable processing possibility.Tortuous groove has constituted a kind of affluent channel between the tributary so, and it works in the enclosure as overflow ducts simultaneously.Therefore this shell can be with low-down expense manufacturing, because avoided disadvantageous undercut thus.Same control assembly can be on a plurality of independent surface of shell pivoting support.
Only when one of use has the control assembly of stationary barrier, be provided with the thrust bearing of supporting control assembly in the enclosure.Control assembly for a high-pressure side forms between two stationary barriers does not need thrust bearing in principle.In a kind of modification in back, show, arrange that on shell the annular chamber that is connected with the high-pressure side is favourable.It allows to carry out better simply sealing at interface area.
Another kind of scheme is that shell is provided with the interface that is used to connect each tube chamber, and is provided with the interface of high-pressure side inlet opening and the interface that low-pressure side flows out opening separately.Therefore the sealing station quantity on annex can drop to minimum.Wherein shell can be provided with one axially and/or the high-pressure side inlet opening of radial arrangement.An axial arranged inflow entrance is opened on the end face that is arranged in shell, and wherein first pipe-line system is arranged on this on high-tension side inlet opening.This structure with simple mode make that the sealing of annex becomes easily because only need the sealing of a static state here.
Another kind of for this reason scheme is that the high-pressure side inlet opening is auxiliary arranges the flow divert device with support member, and the flow divert device just surrounds a bearing of control assembly.This measure helps the shortening of part length and the improvement of rigidity equally.And be arranged on the outer cover owing to have the high-pressure side inlet opening of flow reversing arrangement and supporting, in the possibility of simplifying processing, improved the supporting of control assembly.
Same shell can be provided with and have axially and/or the low-pressure side of radial arrangement outflow opening.
Embodiments of the invention are described in the accompanying drawings, and will further specify below.As shown in the figure
Fig. 1 is according to the equipment of prior art,
Fig. 2 has the cross section of the annex that Fig. 3 a represents to Fig. 7 section,
Fig. 3 a and 3b under first kind of duty, two of annex staggered 90 ° profile,
Fig. 4 a and 4b under second kind of duty, two of annex staggered 90 ° profile, wherein with respect to Fig. 3 a and 3b control assembly separately half-twist draw,
Two 3-D views of Fig. 5 a and 5b annex under cut-away section,
The structure of Fig. 6 drive unit on dividing plate,
The annex of the additional control cylinder of Fig. 7 band,
The annex of two dividing plates of Fig. 8 band,
Fig. 9 under the solid cylinder form with the annex of a control assembly,
Figure 10 a and 10b under first kind of duty, two staggered 90 ° profiles of short annex,
The perspective view of Figure 11 Figure 10 a and 10b control assembly,
Figure 12 is the perspective external view of short annex.
The operation principle of annex has been described on the example of reverse osmosis equipment according to prior art in Fig. 1.High-pressure pump 1 carries liquid to be purified to one or more reverse osmosis membrane assemblies 2, normally lake water, seawater, river bend water or also can be waste water.Osmotic pressure owing to high in membrane module 2 produces separating effect in the film of Bu Zhiing therein.Have purifying waste water of low pressure in the outflow of the back of film, promptly so-called penetrant is collected the back and supplies with other application.
By the unpurified liquid that flows out in the reverse osmosis membrane assembly 2, promptly so-called saline solution after separation process, has the concentration of higher harmful substance, and harmful substance is salt normally, and is flow back to the original place.Because it is with the high energy content of pressure energy form, for energy reclaims, saline solution imports the pressure exchanger in one two chamber by an annex 7.In tube chamber 3.1,3.2, be furnished with under pressure influence movably separator piston 4.1,4.2, it has formed at two separately with the isolation of the cavity of different pressure-loaded.The equipment that has no separator piston tube chamber also is well-known, yet when system was no longer mated by bascule or control time, can cause undesirable mixing between the different liquids inside.
Meanwhile the high pressure of saline solution is pressed on piston 4.1 in first tube chamber 3.1 that is in top shown in Fig. 1 to a side that is in away from annex 7, and transmit pressure everywhere inside and be on the liquid of piston opposite side.Meanwhile high pressure is passed to and is in piston left side and also waits on the low liquid of pressure to be purified.This liquid flows to the left side in upper tube chamber 3.1 with high pressure then, and flows through the check valve 5 of the booster 6 that is arranged in second pipe-line system.Also needing to compensate the small pressure that produces by means of 6 of boosters in the infiltration purification process in membrane module 2 then falls.Because reclaiming 6 of boosters, energy also needs to be provided at the pressure differential that reverse osmosis membrane assembly loses.Therefore high-pressure pump 1 can be very little, and therefore become cheaper than the cost of equipment when not having energy to reclaim.
When in first tube chamber 3.1, when piston 4.1 arrived the tube chamber end, annex 7 switched then, and therefore first tube chamber and atmosphere are connected from now on.Inlet pressure in the intake line of guiding to main pump 1 is enough, with liquid to be purified, being in the saline solution that reduces pressure now in the first top tube chamber 3.1, again by extrusion to the right in the top tube chamber 3.1, and makes one in line in atmosphere.During the process that saline solution is discharged in by first tube chamber 3.1, simultaneously by annex 7, the loading of bottom second tube chamber, 3.2 usefulness high pressure saline solutions.The discharge process of decompression saline solution is described in second tube chamber 3.2 of bottom.
Periodic conversion by corresponding annex 7 realizes that the alternative pressure of two tube chambers 3.1,3.2 loads, and realizes that therefore effective energy reclaims.Because the threeway function in annex may produce compression shock in transfer process, it can damage the diaphragm in the reverse osmosis membrane assembly 2.For making this danger drop to minimum, for this purpose is provided with additional special pressure equalisation openings in the control assembly of annex 7.By adjust during moving in conversion, uncompensated radial displacement meeting brings other rough sledding.
In Fig. 2, by show the cross section A-A and the B-B of two interlaced 90 ° of layouts according to a cross section of annex of the present invention.By means of its help, in ensuing description of drawings, the operation principle of annex is explained.Four-headed arrow Z has shown here by coming in (not shown) pressure exchanger tube chamber and flow direction in the pressure exchanger tube chamber; Single arrow Y has shown the discharge direction by the decompression saline solution that flows out in the annex.
Annex according to the present invention is represented in the section of two interlaced separately 90 ° of layouts in Fig. 3 a and 3b.Fig. 2 is taken from the position of cross section A-A and B-B, and remains constant in the position of the cylindrical control assembly 10 of description of profile hollow core.
Hollow cylinder control assembly 10 is arranged in the shell 11 of annex pivotally.Flow out by reverse osmosis membrane assembly 2, be in the saline solution under the high pressure, be called high pressure saline solution (HPB) below, and,, enter a high pressure chest 14 of annex by a unique high-pressure side inlet opening 12 by means of a gatherer that (not shown) is preposition.This example has represented that an annex is similar to being connected of two-tube pressure exchanger shown in Figure 1 with one.Owing to this reason has been abandoned being connected to describing of tube chamber on the annex.
The shell 11 of annex has two interfaces 16,17 on outer wall 15, (not shown) pipeline that is used to connect same not shown tube chamber 3.1,3.2 just is connected on the top.The embodiment of shell 11 is provided with all-in-one-piece flow channel 18-21 and two ring cavities 26,27 here, is implemented in interface 16,17 and is arranged in the connection between the flow openings 29-36 on the outer casing inner wall 28 by means of their help.Here because structural reason is a hollow cylinder thin wall component, it is arranged in the shell 11 outer casing inner wall 28 hermetically.When it for example made a cast structure, it can be a fixing building block of shell 11 equally.28 whiles of outer casing inner wall are as the radial support of hollow cylinder control assembly 10.The wall of control assembly 10 is passed by a plurality of control opening 37-44.
Shown in Fig. 3 a, enter the high pressure chest 14 of shell 11 by inlet opening 12 by a represented high pressure saline solution of arrow HPB.High pressure chest 14 is arranged within the control assembly 10, and fixedly end face 13 and a dividing plate 47 fence up along axial direction by shell.Dividing plate 47 seals with respect to control assembly 10 by means of seal 49 in the present embodiment.And dividing plate 47 particularly is connected with end face 13 antitorque commentaries on classics here by support bar 48 and shell 11.By this project organization, can during its converting motion, alleviate axial compressive force by rotating control assembly 10.Can find the application scheme of knowing for seal 49.
In control assembly 10, compare here in the enclosure at the control opening 37-40 of the area arrangements of high pressure chest 14 that corresponding to therewith flow openings 30,31,34,35 has other opening angle on the wall 28.Selection by the suitable openings angle can realize, in the transition period of control assembly 10, is in effective (not shown) tube chamber that is connected with annex here by interface 16,17, can instantaneously be in simultaneously under the high pressure of inlet opening 12.Therefore the pressure oscillation that endangers the reverse osmosis equipment film has been avoided.
Control assembly 10 can turn round layout in shell 11.The dividing plate of fixing with support bar 48 antitorque commentaries on classics on shell 11 47 approximately is in the zone line of shell.Dividing plate 47 has become control assembly 10 internal distribution to have two chambeies 14,45 in different pressures district.What chamber 14 here continued is connected with the higher-pressure region HPB of membrane module.Opposite another chamber 45 that in Fig. 3 a, is in dividing plate 47 left sides, with that represent by arrow LPB, decompression, be connected by an interface 46 of the low-pressure area of the saline solution that flows back in the tube chamber.Because control assembly 10 relatively moves for dividing plate 47, so be provided with a seal 49 that is fit to for the pressure condition of sealing.
Control assembly 10 drives by a power transmission shaft 50, and its end is protruding by the through hole 52 on the shell of low-pressure side.Gyration can be continuous or stepping, and speed will depend on that remaining system unit determines.
When the position of control assembly 10 does not change, as follows in the operation principle shown in Fig. 3 a and the 3b according to convert attachments of the present invention:
By axial arranged here unique inlet opening 12, high pressure saline solution HPB flows into high pressure chest 14.This structure decrease the quantity of interface and the cumulative volume of annex.Certainly the supply inlet opening 12 of high pressure saline solution HPB also can radial arrangement, yet the structure of annex just must be longer, and supply must can't realize that control assembly 10 overlapping shell region carry out.Low pressure saline solution LPB from annex is discharged by interface 46.Annex guaranteed basically, from interface 16 and tube chamber that 17 are connected a tube chamber is arranged all the time with the filling of high pressure saline solution, then from the another one tube chamber, the low pressure saline solution of decompression is drained.Only instantaneous two tube chambers in the transition period obtain high pressure simultaneously.
First kind of duty (Fig. 3 a and 3b):
High pressure saline solution HPB is by high pressure chest 14, by in control assembly 10, being in the control opening 38 and 39 of face-to-face position mutually, the control opening 30 and 31 that is in face-to-face position in the enclosure in the wall 28 equally mutually flows into the annular chamber 27 that is integrated in the shell 11, comparison diagram 3b.Two dividing plates 24,25 that partly surround annular chamber 27 along axial direction have formed the supporting of outer casing inner wall 28 simultaneously.High pressure saline solution HPB flows to one first tube chamber interface 17 from annular chamber 27.Remaining is in annex, formed annular chamber 26 and interface 16 flow channel, passage 20 and 21 flow openings 34,35, be closed by control assembly 10.Filled with this first tube chamber that is in interface 17.
Be in effective the connection by interface 16 annexes with two other tube chamber simultaneously.Be back to annex from the low pressure saline solution LPB that second tube chamber, reduces pressure here, and enter annular chamber 26 by interface 16, and by the flow openings 33 and 36 that is in face-to-face position mutually, and, enter low-pressure cavity 45 by in control assembly 10, being in the control opening 41 and 44 of face-to-face position equally mutually.Flow into an interface 46 from that low pressure saline solution LPB that comes out, realize the emptying of tube chamber thus to atmosphere one side.Arrange on all other the wall in the enclosure 28 that guide channel 18 and 19 flow openings 29,32 are closed by control assembly 10.Two in axial direction the part dividing plate 22,23 that surrounds annular chamber 26 constituted another bearing of control assembly 10, comparison diagram 3a simultaneously.
The high pressure saline solution that flows into first tube chamber by interface 17 with its pressure energy pass to be positioned at the inside still wait to be purified, and then be pressed into the liquid of reverse osmosis membrane assembly with higher pressure.The selection in the opening cross section of the speed of gyration of drive unit on power transmission shaft 50 (not shown) and control opening 37-40 has guaranteed that in the moment of tube chamber before being filled with by the high pressure saline solution fully at interface 17 places, injection process finishes.The discharge process of while at second tube chamber at interface 16 places finishes equally.
That concur in pairs separately in the high-pressure side and be in the opening 38/30 and 39/31 of face-to-face position mutually, however than the time of opening at the paired opening 41/33 and 44/36 of low-pressure side to keep long a bit.Thus when paired opening 38/30 and 39/31 is just in time closed, the tube chamber that at this moment is in interface 16 places by paired opening 37/34 and 40/35, passage 20 and 21 and annular chamber 26 obtained high pressure.Therefore guaranteed that second kind of duty begins along with the change of the flow direction that arrives tube chamber under no compression shock.
Second kind of duty (Fig. 4 a/4b):
Opposite with shown in Fig. 3 a and the 3b represent at the half-twist in shell 11 of control assembly 10 shown in this accompanying drawing, and the mobility status to tube chamber is opposite fully at interface 16,17 places.In order better to see clearly, abandoned during rotatablely moving diagram to middle position.
When paired opening 38/30 and 39/31 was in the closed position, the tube chamber of at this moment annotating so continued filling at interface 16 places.On the contrary at the tube chamber at interface 17 places,, be in the passage 18 and 19 and the paired opening 29/42 and 32/43 that is in face-to-face position mutually of face-to-face position mutually, by low-pressure cavity 45 and interface 46 emptyings by annular chamber 27.When the tube chamber at interface 17 places was drained, the pressure energy of high pressure saline solution HPB was delivered in the tube chamber at interface 16 places under second kind of duty.When finishing, be similar to first kind of duty in process, paired opening 37/34 and 40/35 and 38/30 and 39/31 is instantaneously opened simultaneously, proceeds to the transition of the no compression shock of first kind of duty again.
Control assembly 10 is to be provided with seal 49 in the zone of dividing plate 47 on its inside and/or outer circumferential surface here.It has prevented the overcurrent between high-pressure side and low-pressure side, and therefore keeps overall system efficiency.According to the physical dimension of this kind equipment, on control assembly 10, also can use a plurality of such seals 49.
Help by means of it places the power transmission shaft 50 of gyration with control assembly 10, supports by supporting member commonly used, and prevents that by means of the seal of knowing liquid from overflowing.Transmission between power transmission shaft 50 and control assembly 10 realizes by the driving member of knowing 51.It can be support bar, dish or other other device, and it makes from low-pressure cavity 45 to interface 46 fluid by becoming possibility.Fig. 3 a that is introduced in of power realizes at the end face of control assembly 10 in the example shown in the 4b.
Fig. 5 a is a 3-D view on shell that partially opens 11 of annex.The just shell 11 that it is represented does not illustrate the outer casing inner wall 28 of the separation of use in an embodiment.Clearly show that thus, represented this class subchannel by 4 passages 18 to 21 altogether that annular chamber 26,27 sets out, the thin-wall part that it forms in the centre has tortuous variation.Therefore obtained the surface 53 of tortuous variation equally, it is used for the supporting of outer casing inner wall 28 as area supported.The end face of its median septum 22 to 25 or narrow side have the function of area supported simultaneously.Outer casing inner wall 28 also can constitute the integrated component of shell 11.By such flow guide structure, in shell 11, can obtain to be in mutually separately the flow channel or the flow openings of face-to-face position, can realize the motion of control assembly 10 under no radial effect power based on this.
Fig. 5 b has represented to deposit at the cloth corresponding to Fig. 5 a, a section by the annex that assembled, can come into operation.Its adapter 16,17 directly is connected with two tube chambers 3.2,3.1.The hollow cylinder control assembly 10 that has control opening 37-44 turns round in the outer casing inner wall 28 that has flow openings 29-36.The driving of control assembly 10 is undertaken by the power transmission shaft 50 that seals on its end face, act on star driving member 51.Here represent by section, see clearer flow guide device corresponding to the expression of Fig. 3 a and 3b.
Fig. 6 has represented the version according to annex of the present invention of a simplification.Here dividing plate 47 is fixing parts of control assembly 10.The fixing of dividing plate 47 can be undertaken by method commonly used.Dividing plate 47 is integrated components of control assembly 10 in this example, and it can be realized by casting, welding or other engineering type of attachment of knowing.And cancelled thus in Fig. 3 a-4b represented, by means of fixing to dividing plate 47 of the support bar on shell 11.The driving of control assembly 10 is directly carried out on dividing plate 47 by power transmission shaft 50, and other thus otherwise connector 51 that need between power transmission shaft 50 and control assembly 10 has been cancelled.Because dividing plate 47 has been divided into two different pressure areas with the inside of annex, therefore will consider the axial force of caused control assembly 10 from now on.This axial thrust load works along the direction of the high pressure saline solution HPB that flows into high pressure chest 14.It affacts on the dividing plate 47, and produces a component in control assembly.This component can be intercepted and captured with a simple additional thrust bearing spare 54, and imports shell 11.
In Fig. 7, represented at run duration to have to the additional another kind of selectable structure of controlling the annex of possibility of the opening and closing time that changes.An additional control cylinder 55 is between outer casing inner wall 28 and the control assembly 10 with one heart.Control cylinder 55 has the function of an additional hollow cylinder outer casing inner wall, constitutes independent parts, and can rotate with respect to shell with the flow openings that it is inside arranged.It has the control opening 56-63 that other and control assembly 10 are in face-to-face position, it on circumference expansion or exactly it the cross section less than or onesize with the flow openings 29-36 of corresponding outer casing inner wall 28.The suitable selection that flow openings 56-63 by correspondence expands on circumference can influence time of opening or closing of annex by the rotation of control cylinder 55.The adjusting of control cylinder 55 can be carried out by means of hollow shaft 64, it and power transmission shaft 50 concentric runnings, and can regulate by flange 65.Such structure can realize the coupling under the different duties at run duration.Equally also can use other adjusting form.Shown examples of implementation are not limited in such adjusting.
In Fig. 8, represented fixedly connected between control assembly 10 and the dividing plate 47.Control assembly 10 has reached higher rigidity in the zone of high-pressure side and low-pressure side thus.Another dividing plate 66 has been arranged in the axial displacement that occurs in order to deal with in addition, act on the accompanying drawing left side in Fig. 8, and it has sealed high pressure chest 14 to the right in the inside of control assembly 10.This measure has additionally improved rigidity.Driving directly affacts on the dividing plate 47 by power transmission shaft 50 to be carried out.High-pressure side inlet opening 12 is arranged in radially, for this reason control assembly 10 and outer casing inner wall 28 corresponding being extended.High pressure saline solution HPB flows into annular chamber 67 by radial inflow opening 12, flows into outer casing inner wall 28 by two or more flow openings 68,69, and flows into high pressure chest 14 by two or more openings 70,71 in control assembly 10. Opening 70,71 in control assembly 10 is not controlled function in this example, but is similar to an inlet opening 12, only is used for the filling of high pressure chest 14.
Represented a control assembly 10.1 in Fig. 9, it is a solid cylinder.Its rigidity has obtained further raising thus.On the circumferential surface of control assembly 10.1, processed radially relative flow channel 72-73 and 74-75 mutually separately.Therefore be left enough wall thickness between the bottom section of flute profile flow channel 72-75, its thickness is complementary with simple mode and the pressure condition that is stood.In order to prevent the notch stress in control assembly 10.1, the shape of flute profile flow channel 72-75 will be complementary with the material that uses.Be similar to the closure member 10 of hollow cylinder, flow channel 72,73 is carried out the function of high pressure chest, and flow channel 74,75 is carried out the function of low-pressure cavity.High pressure saline solution HPB flows into by the high-pressure side inlet opening 12 of a radial arrangement, and enters a circular passage 76, and it not only can be arranged in the enclosure, perhaps also can be arranged in the control assembly 10.1 as shown in the figure.Circular passage 76 all constitutes complete annular in both cases.Along the relief passage 78 that axial direction passes, be implemented in the pressure-exchange between the axial end surface by means of control assembly 10.1.Meanwhile arranged a free chamber on the on high-tension side end face of control assembly 10.1, the lines that plot runic by the right side are represented in the accompanying drawings, have obtained to be used for the respective surfaces of axial displacement unloading pressure balance thus.
In illustrated layout, high pressure saline solution HPB flows into the circular passage 76 of control assemblies 10.1 by a flow openings in the wall 28 in the enclosure 69, enters the flute profile flow channel 72,73 that in axial direction extends separately from that.The flow openings 30,31,34 and 35 that liquid is mentioned from the accompanying drawing that this high-pressure flow passage 72,73 flows in front.The low pressure saline solution LPB that low pressure flow channel 74,75 in control assembly 10.1 is admitted from the flow openings of mentioning in the accompanying drawing in front 29,32,33 and 36, and be transported to interface 46.Here low pressure saline solution LPB is also always discharged by control assembly 10.1 along axial direction.The space, end that intermeshes separately of flow channel 72-75 is arranged, and formed the ring packing district 77 of a sealing between them.It has prevented the overcurrent between two pressure spans.
Figure 10 a and 10b have represented an annex that has shorter structure length, and represent on the section of two interlaced separately 90 ° of layouts equally.The position class of cross section A-A and B-B is similar to the expression of Fig. 2, and here the position of control assembly 10 also remains unchanged.
According to the annex shown in Figure 10 a and the 10b, arrange to have had shorter structure length by the another kind of flow openings.In shell 11 and in control assembly 10, the position of flow openings 29-36 and control opening 37,40,42,43 is relevant with the plane of the opening of arranging perpendicular to the power transmission shaft 50.2 of control assembly 10 79,80 separately.Embodiment with respect to other has saved two plane of the openings in this embodiment.This form of implementation only has three plane of the openings altogether, 81 inflows that are used for high pressure chest 14 of one of them plane of the opening.When to the inflow of control assembly when axially carrying out, plane of the opening 81 can be cancelled.
In order to save two plane of the openings, in shell, on each comfortable circumference on the plane of the opening 79,80, arranged 4 flow openings, wherein, can see at Figure 10 a split shed the 29,32,34, the 35th.Have among two embodiment that can connect tube chamber at this, in the enclosure on the wall 28, in plane of the opening 79,80, per 4 flow openings 30,31,34,35 or 29,32,33,36 90 ° of layouts that intermesh separately.By means of the control flume 82 that in control assembly 10, is equipped with, high pressure saline solution HPB from one of them plane of the opening 80 along axial direction, by second plane of the opening 79 of control assembly 10 person who lives in exile's shells 11.The function of control flume 82 is seen too clearly by the perspective view of control assembly in Figure 11 10.
Be furnished with additional reinforcement in the inner chamber of hollow cylinder control assembly 10, they are gussets 83,89, and as a kind of current divider that radially extends, along axially passing chamber 14,45.In Figure 10 a, the reinforcement gusset of representing in section 83,89 has extended on the whole diameter of hollow cylinder control assembly 10, and has improved its rigidity in the face of acting on outside and inner and continuing pressure loading alternately.The mutual half-twist in plane along the reinforcement gusset of the direction of power transmission shaft 50.2 trend is arranged, and additionally is directly connected on the dividing plate 47.
Being furnished with reinforcement in the inner chamber of control assembly 10, here is the form with annular element 84.It extends radially inwardly from the inwall of control assembly 10, and stretches into inner chamber 14,45 with the form of ring-type.The also whole rigidity of having improved control assembly 10 of this reinforcement annular element 84.
Inlet opening 12 is the part of outer cover 85 in this embodiment, and outer cover is connected with shell 11 with force transmitted hermetically.Cover structure has this advantage, and shell 11 main compositions own are cylindrical, therefore easier processing.In outer cover 85, be furnished with a flow divert part 86.Be furnished with a plurality of support members 87 in flow divert part 86, it surrounds a plurality of flow channels 88 in outer cover 85.By means of flow divert part 86, the high pressure saline solution HPB that axially enters outer cover 85 is turned to by the flow channel 88 of arc trend, and thus axially or semiaxis to flow into control assembly 10 from the outside, by its opening 70,71 inflow chambers 14.
Control flume 82 37,40 that be connected with the control opening, that form fork-shaped here is arranged on the excircle of control assembly 10, and is in radially relative position mutually.It extends in the both sides of the reinforcement gusset 83 of low-pressure cavity 45, and can only see a part in diagram in this embodiment.In outer cover 85, be furnished with the bearing part 90 and the seal 91 of control assembly 10 in addition.
In the outer wall 15 of shell 10, be furnished with a plurality of access portal 92, it by locking member 93 airtight with the sealing of liquid sealing.Access portal 92 is because process technology former thereby be provided with, and makes the processing of shell become easy significantly.It makes and can easily enter the cavity in the shell of being under annular chamber 26,27 forms.
Figure 10 b has represented a longitudinal profile of arranging with respect to Figure 10 a half-twist.Thus in control assembly 10 as can be seen, strengthen gusset 83 and vertically be in the diagram plane now, and according to the kind of arrangements of flow passage component in low-pressure cavity 45.Opposite on the right side of dividing plate 47, the reinforcement gusset 89 that is in the high pressure chest 14 is in the diagram plane now.Among the represented embodiment, strengthen gusset the 83, the 89th here, the integrated component of dividing plate 47, wherein strengthening gusset 83 also is simultaneously the part that is in the power transmission shaft parts 50.2 in the control assembly 10.This designs simplification its processing.Be equally well that reinforcement is not having can be arranged in the chamber 14,45 under directly effective situation about being connected with dividing plate 47 yet.
Combine as can be seen by two Figure 10 a, 10b, in the zone in chamber 45, in plane of the opening 79, united all control and flow openings 41-44 and 29,32,33,36.In the zone in chamber 14, control and flow openings 37-40 and 30,31,34,35 in plane of the opening 80, have similarly been united.Plane of the opening 81 only is used for the HPB radial inflow to the chamber 14, and does not participate in transfer process.Therefore whole embodiment has obtained obvious shortening, and the rigidity of whole annex is significantly improved.
Figure 11 has represented a perspective view according to the hollow cylinder control assembly 10 shown in Figure 10 a, the 10b.This is to have the drive shaft members 50.2 of stretching out from chamber 45, at the view of the low-pressure side of control assembly 10.The gusset 83 that is arranged in the chamber 45 is high-visible, and its trend is along flow direction or along the direction of power transmission shaft 50.2.Can see that is in addition strengthened an annular element 84, it is around being arranged in the low-pressure cavity 45, in its zone, outflow side.On the circumferential wall surface of control assembly 10, arranging a plurality of relief passages 78 along axial trend.By means of they the help balance axial displacement load, support thus and obviously simplified.
On the outer circumference surface of control assembly 10, be furnished with constitute fork-shaped and be in the radially control flume 82 of relative position, it is connected with control opening 37,40 with the chamber 14 of high pressure saline solution HPB loading.By control flume in the flow divert that realizes on the outer circumference surface of control assembly 10 being connected between two tube chambers of the pressure exchanger on the annex.By means of this measure, in the side of low pressure saline solution LPB, all controls and flow openings can only be displaced in the plane of the opening 79.
The structure of the control flume 82 under the fork-shaped form has this advantage, has stayed an arcuate member 96 between the fork-shaped flow channel that forms thus.It is arranged in the plane of strengthening gusset 83 in an advantageous manner, has optimized power transmission and surface pressing between rotating control assembly and shell thus.In step-like control flume 82, abandoned the layout of arcuate member 96.Though it has enlarged the chamber that is used to turn to, yet caused somewhat disadvantageous mobility status during control assembly 10 converting motions.
No longer carry out control flume motion is turned to the description of this type here.With along with the similar structure of control assembly 10 rotating control flumes in, control flume just also can be arranged in the shell with the form of static mobile groove so.Saline solution enters into the flow divert of plane of the opening 79 so just at shell wall, and is to carry out in static mobile groove.
The opening 70,71 that distributes and arrange can be seen in zone in the chamber 14 that loads with high pressure saline solution HPB on circumference on control assembly 10.High pressure saline solution HPB is by flowing through after (not shown here) flow divert in outer cover thus, by radially or semiaxis flow into the chamber 14 of control assembly from outside to inside to direction.
In Figure 12, represented a perspective view according to an annex shown in Figure 10-11.In outer shell outer wall 15, access portal 92 is high-visible, and it is arranged along the direction of axially moving towards the plane that is in the overflow ducts in the shell.Use simple locking embolism in an embodiment as locking member 93, yet wherein also can adopt other version.Be between the overflow ducts 18-21 in the shell wall 15, in shell 11, be furnished with additional externally reinforced 94.
Be furnished with the additional impression 95 that gathers on the outer wall 15 of shell 11, it has the function of base element and/or suspender for annex.It has been simplified the installation of annex and has made carrying easier.In this embodiment, the interface 46 that plays the effect of low pressure saline solution outlet is parts of independent outer cover part.Thus can the simplest mode, and arrange by the corresponding rotation of outer cover part, the outflow direction of low pressure saline solution LPB can be simply be complementary with different local circumstance by interface 46.
Reference numeral
1 high-pressure pump 50-50.2 power transmission shaft
2 reverse osmosis membrane assemblies, 51 driving members
3.1,3.2 tube chambers, 52 outer shell passage
4.1,4.2 separator pistons, 53 surfaces, area supported
5 check valves, 54 thrust bearings
6 boosters, 55 control cylinders
7 annex 56-63 flow opening
8 64 hollow shafts
9 65 flanges
10,10.1 control assemblies, 66 dividing plates
11 shells, 67 annular chambers
12 inlet opening 68-69 flow openings
13 end-face wall 70-71 openings
14 chambeies, high pressure chest 72-75 flow channel
15 outer walls, 76 circular passages
16 tube chamber interfaces, 77 seal areas
17 tube chamber interfaces, 78 relief passages
18-21 flow channel 79-81 plane of the opening
22-25 dividing plate 82 control flumes
26-27 annular chamber 83 is strengthened gusset
28 outer casing inner walls, 84 annular elements, reinforcement
29-36.1 flow openings 85 outer covers
37-44 control opening 86 flow divert
45 chambeies, low-pressure cavity 87 guiding gussets
46 interfaces, 88 flow channels
47 dividing plates 89 are strengthened gusset
90 supportings of 48 support bars
91 sealings of 49 seals
92 access portal, 93 locking members
94 girth members 95 gather impression
96 arcuate member LPB low pressure saline solutions
HPB high pressure saline solution

Claims (51)

1. the annex that is used for the fluid passage conversion, it is used to have the pressure exchanger equipment of the tube chamber (3) that is provided with alternating current and crosses, wherein in a shell (11), be furnished with one have a plurality of flow channels can rotating control assembly (10,10.1), shell (11) has the interface (12 of a plurality of connecting lines, 16,17,46), wherein shell (11) is connected with first pipe-line system, and by interface (16,17) be connected with at least one pressure exchanger end face separately, wherein pressure exchanger another end face separately is connected with second pipe-line system under the transfer of other annex, control assembly (10,10.1) a motor-driven power transmission shaft (50) is housed, and control assembly (10,10.1) flow channel alternately and go up the interface of arranging at shell (11) and be connected, and along with control assembly (10,10.1) the position of the switch, the highly pressurised liquid that flows into replaces flows to pressure exchanger, and arrive the interface that flows out low pressure liquid by the low pressure liquid that pressure exchanger flows out, it is characterized in that, be furnished with the interface (12) of the highly pressurised liquid (HPB) of an inflow, interface (46) and at least two the pressure exchanger interfaces (16 that alternately load that flow into low pressure liquid (LPB) with highly pressurised liquid and low pressure liquid, 17), in shell (11), realize by axial and/or radial direction to control assembly (10,10.1) inflow, and realize from control assembly (10,10.1) outflow of in axial direction arriving the low pressure liquid of low pressure liquid interface, and at control assembly (10,10.1) transition period, give with annex and be in of the high pressure loading of effective tube chamber that is connected with inlet opening, at control assembly (10,10.1) on the control opening (37-40) of area arrangements of high pressure chest (14) with the flow openings (30 of corresponding to shell (11) therewith, 31,34,35) compare, have an other opening angle.
2. annex according to claim 1, it is characterized in that, described control assembly is the control assembly (10) of a hollow cylinder, and a dividing plate (47) is divided into the control assembly of hollow cylinder (10) in the chamber (14,45) of two different pressures districts (HPB, LPB).
3. annex according to claim 2 is characterized in that, arranges additional reinforcement in the chamber (14,45) of described different pressures district (HPB, LPB).
4. annex according to claim 3 is characterized in that, described this reinforcement can be the gusset (83,89) that radially moves towards and/or make annular element (84).
5. according to claim 2 or 3 described annexes, it is characterized in that described power transmission shaft (50) can transmit moment of torsion with dividing plate (47) employing and be connected.
6. annex according to claim 5 is characterized in that, described dividing plate (47) is arranged in the mesozone of hollow cylinder control assembly (10).
7. according to each described annex in the claim 1 to 3, it is characterized in that the parts (51) that can transmit moment of torsion are arranged on the end face of hollow cylinder control assembly (10).
8. according to claim 2 or 3 described annexes, it is characterized in that described dividing plate (47) is fixedlyed connected with control assembly (10).
9. according to claim 2 or 3 described annexes, it is characterized in that described dividing plate (47) is fixedlyed connected with shell (11).
10. annex according to claim 9 is characterized in that, in high-pressure side inlet opening (12) district, described dividing plate (47) is fixed on the shell (11) with support bar (48).
11., it is characterized in that the seal (49) between described dividing plate (47) and hollow cylinder control assembly (10) inner wall surface is arranged in a seal area according to claim 2 or 3 described annexes.
12. annex according to claim 10 is characterized in that, described dividing plate (47) and/or described support bar (48) are interchangeable parts.
13. annex according to claim 1 is characterized in that, described control assembly (10.1) is a solid cylinder, and a plurality of flute profile flow channels (72-74) constitute different pressures district (HPB, LPB) on its circumferential surface.
14. annex according to claim 13 is characterized in that, on described circumferential surface, and the flow channel (72,73 of same pressure area; 74,75) mutual radially relative face-to-face layout.
15., it is characterized in that a cross section of the flute profile flow channel (72-75) that links to each other with the flow openings (29-31,33-35) of described shell has formed the control opening of control assembly (10.1) according to claim 13 or 14 described annexes.
16. according to claim 13 or 14 described annexes, it is characterized in that,, in shell (11) and/or in the circumferential surface of control assembly (10.1), arranged a cannelure (76) in the zone of the inlet opening in high-pressure side (69) radially.
17. according to claim 13 or 14 described annexes, it is characterized in that, on described control assembly (10.1), between the end of the flute profile flow channel (72-75) of different pressures district (HPB, LPB), be furnished with the ring packing district (77) of a sealing.
18. annex according to claim 17 is characterized in that, the zone in seal area (77) is gone up and/or be furnished with seal on shell (11) at control assembly (10.1).
19. according to claim 1,2 or 13 described annexes, it is characterized in that, on the outer circumference surface of described control assembly (10,10.1), be furnished with the formation fork-shaped and/or control flume (82) step-like and that be connected with control opening (37,40).
20. annex according to claim 4, it is characterized in that, be furnished with the formation fork-shaped on the outer circumference surface of described control assembly (10,10.1) and control flume (82) that be connected with control opening (37,40), the arcuate member (96) of described fork-shaped control flume (82) is arranged in the plane of described radially gusset (83).
21. according to each described annex in the claim 1 to 3, it is characterized in that, on the inner peripheral surface of described outer casing inner wall (28,55), be furnished with fork-shaped and/or the mobile groove step-like and that be connected with flow openings (30,31,34,35) of formation.
22. according to each described annex in the claim 1 to 3, it is characterized in that, the outer wall (15) of described shell (11) go up and/or in be furnished with the overflow ducts (18-21) of a plurality of connection flow openings (29-31,33-36).
23. annex according to claim 22 is characterized in that, described flow openings (29-31,33-36) is the part of an adjustable hollow cylinder outer casing inner wall (55).
24. according to each described annex in the claim 1 to 3, it is characterized in that, in the outer wall (15) of described shell (11), be furnished with a plurality of access portal (92).
25. according to each described annex in the claim 1 to 3, it is characterized in that, in the outer wall (15) of described shell (11), be furnished with the reinforcement (94) of a plurality of outsides.
26. annex according to claim 22 is characterized in that, the tube chamber of described pressure exchanger (3.1,3.2) is instantaneous during control assembly (10,10.1) moves to interconnect by overflow ducts (18-21).
27. annex according to claim 22 is characterized in that, described overflow ducts (18-21) is an outer tube.
28. annex according to claim 27 is characterized in that, is arranging the pipe fitting interface on the outer circumference surface of described shell (11).
29. annex according to claim 22 is characterized in that, described overflow ducts (18-21) is the flow channel that is integrated in the shell wall.
30. according to each described annex in the claim 1 to 3, it is characterized in that, by minimum two flow openings (29,32 that radially are in mutually face-to-face position relatively separately; 30,31; 33,36; 34,35), and corresponding to therewith control opening (37-44) be implemented in fluid exchange between control assembly (10,10.1) and the overflow ducts (18-21).
31., it is characterized in that the position of described control opening (37-44) and size make no compression shock flow and be converted into possibility according to each described annex in the claim 1 to 3.
32. annex according to claim 31 is characterized in that, the control opening (37-44) of described hollow cylinder control assembly can be slot, polygon or dihedral.
33. annex according to claim 31 is characterized in that, closing of a tube chamber control opening links with the opening mutually of control opening of another tube chamber of closing previously simultaneously, and vice-versa.
34. according to each described annex in the claim 1 to 3, it is characterized in that, on the outer wall surface of described control assembly (10,10.1) and/or be on the case surface of face-to-face position, perhaps be furnished with a plurality of relief passages in the wall (28,55) in the enclosure.
35. according to each described annex in the claim 1 to 3, it is characterized in that, in described control assembly (10,10.1), be furnished with one or more relief passages (78).
36. annex according to claim 34 is characterized in that, realizes flowing through continuously or alternately in described relief passage.
37. according to each described annex in the claim 1 to 3, it is characterized in that, described control assembly (10,10.1) be bearing in a tortuous trend, by on the end face of dividing plate (22-25) surface (53) that form, shell (11).
38., it is characterized in that described control assembly (10,10.1) is bearing in by on the end face of dividing plate (22-25) a plurality of surfaces (53) that form, shell (11) according to each described annex in the claim 1 to 3.
39. according to each described annex in the claim 1 to 3, it is characterized in that, an outer casing inner wall (28) that constitutes as separate part be bearing in tortuous trend, by on the end face of dividing plate (22-25) surface (53) that form, shell (11).
40., it is characterized in that described control assembly (10,10.1) is arranged in the bearing (90) with at least one axle journal according to each described annex in the claim 1 to 3.
41., it is characterized in that the layout of control assembly (10,10.1) is bearing radial force and axial force not according to each described annex in the claim 1 to 3.
42., it is characterized in that a hollow cylinder control assembly (10,10.1) that has stationary barrier (47) is close on the thrust bearing (54) according to each described annex in the claim 1 to 3.
43. according to each described annex in the claim 1 to 3, it is characterized in that, on described control assembly (10,10.1), between two stationary barriers (47,66), form high-pressure side (HPB).
44., it is characterized in that an annular chamber (67) of Bu Zhiing is connected with high-pressure side (HPB) in the enclosure according to the described annex of claim 41.
45. according to each described annex in the claim 1 to 3, it is characterized in that, described shell (11) is provided with and is respectively applied for the interface (16,17) that connects tube chamber (3), and described shell (11) is provided with an interface that is used for a high-pressure side inlet opening (12) and is used for the interface that a low-pressure side flows out opening (46).
46. according to the described annex of claim 45, it is characterized in that, described inlet opening (12) is auxiliary arranges the flow divert (86) with support member (87), and flow divert (86) just surrounds a bearing (90) of control assembly (10,10.1).
47., it is characterized in that the described inlet opening (12) that has flow commutation (86) and bearing (90) is arranged in the outer cover (85) that is connected with shell (11) according to the described annex of claim 46.
48. according to the described annex of claim 45, it is characterized in that, described shell be provided with have one axially and/or the low-pressure side of radial arrangement flow out opening (46).
49. annex according to claim 1 and 2 is characterized in that, described control assembly is a hollow cylinder, and the control opening (37-44) of this hollow cylinder control assembly is slot, polygon or dihedral.
50. annex according to claim 30 is characterized in that, the control opening (37-44) of described hollow cylinder control assembly is slot, polygon or dihedral.
51. annex according to claim 35 is characterized in that, realizes flowing through continuously or alternately in described relief passage.
CNB2004800064417A 2003-03-12 2004-02-18 Fitting for installations having pressure exchangers Expired - Fee Related CN100404112C (en)

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DE10310663 2003-03-12
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US4705625A (en) * 1985-10-31 1987-11-10 Hart Jr John E Reverse osmosis water purifying system
GB2204664A (en) * 1986-05-15 1988-11-16 Oceanic Systems Limited Spool valves
US5306428A (en) * 1992-10-29 1994-04-26 Tonner John B Method of recovering energy from reverse osmosis waste streams
EP1095693A1 (en) * 1998-06-30 2001-05-02 Manuel Barreto Avero Water desalting installation through reverse osmosis with pressurized supply tanks in continuous kinetic cycle

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* Cited by examiner, † Cited by third party
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GB915827A (en) * 1960-08-16 1963-01-16 Power Jets Res & Dev Ltd Improvements in or relating to pressure exchangers
US4705625A (en) * 1985-10-31 1987-11-10 Hart Jr John E Reverse osmosis water purifying system
GB2204664A (en) * 1986-05-15 1988-11-16 Oceanic Systems Limited Spool valves
US5306428A (en) * 1992-10-29 1994-04-26 Tonner John B Method of recovering energy from reverse osmosis waste streams
EP1095693A1 (en) * 1998-06-30 2001-05-02 Manuel Barreto Avero Water desalting installation through reverse osmosis with pressurized supply tanks in continuous kinetic cycle

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