Patent Application
20130168307
The disclosure is directed to multi membrane pressure vessel with integrated bottom distribution and top collector system.
Ultrafiltration is a type of filtration, other types of filtration may be microfiltration or nanofiltration. Ultrafiltration is employed to separate or remove particles larger than sizes of about 0.01-0.1 μm—depending upon the pore sizes of the ultrafiltration unit—in order to purify or to recycle a fluid flow. Ultrafiltration (abbreviation: UF) is a variety of membrane filtration in which typically hydrostatic pressure forces a liquid against a semipermeable membrane. Suspended solids and solutes of high molecular weight are retained, while water and low molecular weight solutes pass through the membrane.
Ultrafiltration is a separation process using membranes with pore sizes typically in the range of 0.1 to 0.001 micron. Ultrafiltration allows to purify, separate, and concentrate target macromolecules in continuous systems. This is done by pressurising the solution flow and guiding this pressurised solution through an ultrafiltration membrane. The solvent and other dissolved components that pass through the membrane are known as “permeate”. The components that do not pass through are known as “retentate”. Depending on the pore sizes of the membrane used in relation to the particle sizes, macromolecules may be purified, separated, or concentrated in either fraction.
In certain conventional products, water treatment is done by a plurality of ultrafiltration modules, each module may be substantially a cylinder comprising one or several ultrafiltration membranes. The membrane may be mainly of capillary and/or hollow fibre type. Each module may have its own housing with connectors for fluid supply or fluid drain.
For industrial large scale filtration systems, e.g. for purifying a large amount of water, a plurality of these modules are provided for one filtration system. Typically they are arranged in rows and columns, typically in parallel configuration, each module having a separate inlet and outlet tubes to provide a fluid flow through the module. A typical arrangement can be seen schematically in
To provide a sufficient filtration throughput, the overall filtration system requires a large filtering surface which can be reached by a necessary number of filtration modules. This may lead to a large footprint of the overall filtration system.
Thus, it is a goal to provide a modified ultrafiltration system that results in a more compact arrangement.
In one embodiment, a pressurised filtration vessel, e.g., in cylindrical form, comprises: a filter element, comprised of a plurality of filtration membrane modules, particularly ultrafiltration membrane modules; a distributor connected to an inlet for distributing an input fluid to the filter element; a collector connected to an outlet for collecting an output fluid from the filter element; wherein the filter element is located between the distributor and the collector.
In a further embodiment, the distributor is arranged substantially as an elliptic paraboloid with an opening for connection to the inlet at a tip of the elliptic paraboloid; and/or the collector is arranged substantially as an elliptic paraboloid with an opening for connection to the outlet at a tip of the elliptic paraboloid. In a further embodiment, the plurality of filtration membrane modules are positioned at a first end via a support plate and at a second end via a retaining plate. In a further embodiment, the retaining plate and/or the support plate is arranged as a disc with recesses, each recess having the size of a cross section of one of the plurality of filtration membrane modules, the cross section being perpendicular to an axis of the respective filtration membrane module. In a further embodiment, a guide plate is arranged as a disc with blanked out punchings, each punching having the size of a cross section of one of the plurality of filtration membrane modules, the cross section being perpendicular to an axis of the respective filtration membrane module. In a further embodiment, the plurality of filtration membrane modules each have cylindrical form and are arranged parallel to each other, such that the filtration membrane modules being arranged in a substantially honeycomb-like structure. In a further embodiment, the distributor is arranged to guide the input fluid to cylindrical outer surfaces of the plurality of filtration membrane modules. In a further embodiment, the plurality of filtration membrane modules are configured that to be filtered fluid is fed via the cylindrical outer surfaces. In a further embodiment, the collector is arranged to guide filtered fluid discharged from circular top surfaces of the plurality of filtration membrane modules to the outlet as the output fluid. In a further embodiment, the plurality of filtration membrane modules are configured that to be filtered fluid is filtered by membranes of the plurality of filtration membrane modules and that the filtered fluid is guided to the circular top surfaces of the plurality of filtration membrane modules for discharge. In a further embodiment, the collector is arranged such that the output fluid is funnelled into a nozzle during operation. In a further embodiment, the plurality of filtration membrane modules each comprising a plurality of filtration membranes. In a further embodiment, each of the filtration membrane modules is in cylindrical form. In a further embodiment, a scouring plate is provided, the scouring plate providing air holes directed to a surface of the filtration membrane modules. In a further embodiment, the vessel further comprises air channels for air scouring and or channels to return cleaning fluid during backwash.
Example embodiments will be explained in more detail below with reference to figures, in which:
Some embodiments provide a pressurised filtration vessel, e.g., in cylindrical form, which comprises a filter element for filtering an input fluid, a distributor, and a collector. The distributor is connected to an inlet for distributing the input fluid to the filter element. The collector is connected to an outlet for collecting an output fluid from the filter element. The filter element is located between the distributor and the collector, and the filter element may comprise a plurality of filtration membrane modules, particularly ultrafiltration membrane modules. The filtration vessel may particularly be an ultrafiltration vessel.
During operation, a to be filtered liquid or multiphase fluid—the input fluid—may be supplied under pressure to the distributor. The distributor may be arranged such that the fluid is distributed to all of the plurality of filtration membrane modules. The same amount of fluid may be supplied to all of the surfaces of each of the filtration membrane modules.
In one embodiment the distributor may be arranged substantially as an elliptic paraboloid with an opening for connection to the inlet at a tip of the elliptic paraboloid. At the time of filing of this patent application an example of an elliptic paraboloid can be seen on the web page http://mathworld.wolfram.com//EllipticParaboloid.html or is known substantially from the form of satellite dishes to define what is meant by the term elliptic paraboloid.
The distributor and the collector may be each built as a single piece, i.e., formed integrally. Specifically a system of pipes may not be considered to be a distributor or a collector according to the present disclosure. The distributor and the collector may be free of pipes, i.e., pipe-less.
Each of the plurality of filtration membrane modules may comprise a plurality of filtration membranes for filtering the input fluid, each of the filtration membranes may be in cylindrical form and may be built from carbon and/or fibre to provide the filtering effect. The to be filtered input fluid may be provided to the filtration membrane via its cylindrical side surface such that the fluid can—in parts without the to be filtered particles—pass radially inwards into the body of the filtration membrane.
Purified fluid passing the filtration membranes—the output fluid, will reach the collector via which the fluid collected and distributed to the outlet.
This arrangement allows a filtration of a fluid with a very compact design, as all filtration membrane modules are arranged in a single vessel. Only a single housing may be necessary for the overall vessel and no specific housing is necessary for the filtration membrane modules. As the distribution and collection of the fluid is done by single elements—the distributor and the collector—without using a system of pipes, a very fail-safe system can be provided via which leakages from the pipes can be avoided or at least reduced. The number of parts can be reduced significantly. The footprint and the weight of the vessel may be less than a conventional solution.
Nevertheless the vessel remains a modular design. Installation of the vessel may be quick and easy. The vessel may be installed from pre-assembled parts.
In one embodiment the vessel is wherein the plurality of filtration membrane modules may positioned on a first end via a retaining plate and on a second end via a support plate. The first end is the end in direction of the inlet, the second end the end in direction of the outlet. This allows having a very robust and stiff implementation by only using little material as support structure.
The retaining plate and/or the support plate may possibly be arranged as a disc with recesses, each recess having the size of a cross section of one of the plurality of filtration membrane modules, the cross section being perpendicular to an axis of the respective filtration membrane module. Typically the retaining plate and the support plate may be substantially similar in overall form, but typically will differ in regards of the position and occurrence of through holes.
In another embodiment a guide plate may be present between the first end and the second end. The guide plate may be arranged as a disc comprising blanked out punchings, each punching having the size of a cross section of one of the plurality of filtration membrane modules, the cross section being perpendicular to an axis of the respective filtration membrane module. A filtration membrane module may be cylindrical and a respective punching may be circular. Such a guide plate may provide a wanted stiffness of the vessel structure. Besides, a guide plate may give support or guidance for inserting the filtration membrane modules.
With the punchings and/or the recesses it is possible to keep the plurality of filtration membrane modules in position, e.g., parallel to each other.
The recesses of one of the support plates may each have a central hole through which the output fluid may be guided to the outlet.
The recesses of one of the support plates may each have a small central hole through which fluid may be guided to drain the filtration membrane modules.
In a further embodiment the plurality of filtration membrane modules may each have cylindrical form and may be arranged parallel to each other, such that the filtration membrane modules may be arranged in a substantially honeycomb-like or grid-like or hexagonal structure. The filtration membrane modules may be fixed via the punchings and/or the recesses that are arranged in the substantially honeycomb-like or grid-like or hexagonal structure. The punchings and/or recesses may be staggered, e.g., staggered by the radius of the cylindrical filtration membrane modules.
This may be advantageous as this may allow a very compact design as the distance between the filtration membrane modules can be minimised. Therefore such a compact vessel can even be used in space restricted areas, like offshore installations. Offshore installations may be oil or gas platforms, installations on the sea bed, or on ships. Nevertheless the compact design may also be considered advantageous for onshore installations.
In one implementation, the collector may be arranged such that the output fluid is funnelled into a nozzle during operation. For this the collector may have depressions or corrugations. The collector may also be a dish of concave form with a central opening as an outlet for the fluid. This dish may have ribs so that the collector becomes more rigid. In other words, the collector may be arranged substantially as an elliptic paraboloid with an opening for connection to the outlet at a tip of the elliptic paraboloid.
The distributor may also have depressions or corrugations. Both the distributor and the collector may be substantially of the same shape and may even be identical parts. They may be assembled in opposite orientation to each other.
The fluid may be provided to the vessel under pressure. Besides, the filtration membranes may be oriented vertically such that may also operate gravity-driven.
Ultra filtration membranes for water treatment are usually directed for onshore needs. Such type of filtration membranes can possibly be disadvantageous in one of the following respects, as they are typically arranged in a design like it is shown in
Such a filtration system may be composed of filtration membrane modules, which may be a pressurised, pre-engineered membrane system. A modular “building block” configuration can simplify design, reduces installation and makes operation easy. A hollow-fibre technology may be used to provide a verifiable barrier, assuring virus, turbidity, suspended solids, and pathogen removal. For example a system may allow up to 40 million liters per day of treated water capacity on one skid.
The filtration system may be a gravity-driven system.
It may replace systems that require coagulants for pre-treatment of fluid provided to reverse osmosis applications such as treatment of drinking water, desalination, reuse and industrial applications.
A manifold system may be needed to distribute and collect fluids, isolate individual modules or pre-load membrane modules. It is advantageous if components are interchangeable. The manifold system may be an external distribution and collecting system containing numerous parts, like pipes and conduits.
As an example, a system described above may have a design pressure of 6 bar (i.e. 6*105 Pa) above the atmospheric pressure.
A new inventive arrangement is proposed based on
The to be discussed filtration vessel may be an ultrafiltration vessel, but possibly concepts of this vessel may also be applied to other types of filtration as long as no obstacles are present that would stop a skilled person to apply the disclosed technology also to other forms of filtration, like microfiltration, nanofiltration, or even reverse osmosis.
Referring now to
It is assumed that the vessel 1 is oriented in a vertical way. The vessel may be symmetric about an axis Al. The internal structure of the vessel 1 may not be perfectly axial symmetric, as a plurality of filtration membrane modules 3 will be present within a body of the vessel 1. The filtration membrane modules 3 may be arranged such that they may be located point symmetric about the axis or may be mirror symmetric in respect to a plane defined by the axis A1 and a radial component perpendicular to the axis A1.
In the following the components of the vessel are explained in the order as they are located from top to bottom—in reverse of the fluid flow when in filtering operation. A top portion of the vessel comprises a lock nut 101, a spacer 102, a locking ring 105, a dished endcap 104, a collection manifold 105 as a distributor, a removable nozzle gasket 106, a removable nozzle 107 as an outlet, a retaining plate top gasket 108, a retailing plate 109, a retaining plate gasket 110, a membrane seal gasket 111, locating pins 112.
The removable nozzle 107 is providing a connection to a pipe system such that the filtered fluid can be guided away via the pipe system. The fluid may be the filtered liquid or multiphase solution which at this stage is cleared from included particles, viruses, etc.
The dished endcap 104 may be considered part of an external housing 215 of the vessel 1.
The collection manifold 105 may be in form of a dish with some ribs in the recess to guide and distribute the fluid to a plurality of filtration membrane modules 3 as filter element 2.
During operation the fluid will be discharged at the filtration membrane modules 3 via a top end of the respective filtration membrane module 3. The fluid will pass through a plurality of holes in the retaining plate 109, which has cylindrical recesses, each recess configured to match a top end of a corresponding filtration membrane module 3.
For each recess in the retaining plate 109, a corresponding filtration membrane module 3 is present, that has a top end that matches the form of the recess of the retaining plate 109.The filtration membrane modules 3 are configured such that the filtered fluid can be discharged via its top end.
Each filtration membrane module 3 may be substantially symmetric about an axis A2 and may be comprised of a plurality of cylindrical hollow fibre elements for filtering the fluid. Alternatively other ways of filtering may be used within the filtration membrane module 3. Filtering may take place by providing the to be filtered multiphase fluid to the outside of the cylindrical hollow fibre under pressure. “Pure” fluid will pass through. Solids may be retained.
In an axially central region of the filtration membrane modules 3, the vessel 1 may also comprise one or several guide plates 114 that provide a support for the elongated filtration membrane modules 3. The guide plate gasket 113 may have a disk-like shape. Its outer radial surface may be connected to the housing 215. The guide plate 114 may have a plurality of punchings 120 that each correspond to an outer surface structure of the filtration membrane module 3.
The locating pins 112 may be present for alignment of the collection manifold 105 and/or the retaining plate 109 and/or the guide plate 113.
Continuing to describe the vessel 1 from top to bottom, following the plurality of filtration membrane modules 3 a fairly similar design is present as described before, only in a reverse order. The plurality of filtration membrane modules 3 may be followed by a support plate gasket 216 and a support plate 217. The vessel 1 then further comprises removable nozzle 207, a removable nozzle gasket 206, a distribution manifold 205, a dished endcap 204, a locking ring 203, a spacer 202, and a lock nut 201.
The to be filtered fluid may be fed to the vessel 1 from the bottom end. It will enter the vessel 1 and will be distributed by the distribution manifold 205 to the side surfaces of the filtration membrane modules 3. Bottom ends of the filtration membrane modules 3 are caught by opposing recesses 220, which each may have drain holes. Furthermore the support plate 217 may have feeding holes to let pass the to be filtered fluid from a “basin” of the distribution manifold 205.
The distribution manifold 205 may distribute the fluid overall the cross section of the vessel 1 due to its concave form. The distribution manifold 205 may have ribs to guide the fluid from a central hole of the distribution manifold 205 and/or to provide stiffness to the distribution manifold 205.
The dished endcap 104 may be considered part of the external housing 215 of the vessel 1, the dished endcap 104 closing the vessel 1 in axial direction.
The described components are surrounded by the cylindrical housing 215, which may be of carbon fibre or epoxy and which may close the vessel 1 in radial direction along it axial stretch.
The removable nozzle 207 is providing a connection to a pipe system for the to be filtered fluid which is external to the vessel 1. The fluid may be provided by a tank or a supply and may be the to be filtered liquid or multiphase solution which may include particles, viruses, etc. The fluid as provided to the vessel 1 may be pressurised.
Once assembled and in operation, a to be purified fluid will enter the vessel 1 from the bottom via the removable nozzle 207. The fluid will be spread in radial direction by the distribution manifold 105, passing through holes within the support plate 217, so that the fluid is provided to all the present filtration membrane modules 3. By passing through the side walls of the filtration membrane modules 3 and through filtration membrane modules 3 the fluid will be filtered. Particles of a size greater than a given threshold will be withheld on the surface of or in the filtration membrane modules 3. The purified fluid will be exiting the filtration membrane modules 3 at its top ends, passing into the collection manifold 105 via holes in the retaining plate 109. The collection manifold 105 will collect the filtered fluid like a funnel and will provide the fluid via a central hole to the removable nozzle 107, so that the filtered fluid can be guided away via a system of pipes.
The collection manifold 105 may have ribs to guide the fluid to the central hole of the collection manifold 105 and/or to provide stiffness to the collection manifold 105.
In
In
A collector and/or a distributor may be a substantially dish-like body, having an outer rotational symmetrical convex surface and an inner concave surface, and a central hole. Comb-like ribs may be present that extend from a circular rim in radial inward direction, the rim and the ribs forming a flat surface with recessions in between the ribs. The ribs particularly do not extend from one end of the rim to another end but may be noncontinuous. Particularly, a plane of symmetry can be defined, such that the collector is axial symmetric to the plane of symmetry. The ribs then look like two combs facing each other with their teeth. Additionally, the ribs particularly may extend axially from the flat surface to the inner concave surface.
The collector may be arranged to be able to discharged fluid via its central hole, the fluid entering from the wide end of the collector.
The distributor may be arranged substantially the same as the collector, but arranged opposite to the collector during operation, such that fluid entering via its central hole will be discharged via its wide end.
The form of the ribs of the collector or distributor may be adapted to the form of an adjacent support plate or retaining plate.
Another implementation of a distributor will later be seen in
The support plate may be a disc with a plurality of recesses, with a hole in the centre of each recess. The recesses show a honeycomb-like structure, even though the recesses may be circular disc-like cavities. Recesses may be arranged as close as possible to each other to obtain a maximum possible packing density. The recesses should show a matching form of an end of the filtration membrane modules, which may be cylindrical. The radial surfaces of the retaining plate may lie merely in three different planes parallel to each other.
The retaining plate may be arranged substantially the same as the support plate, but arranged opposite to the support plate to clamp or lock the plurality of filtration membrane modules in between.
The guide plate may be arranged substantially the same as the support plate, but only differing that the recesses are replaced by through holes with substantially the same shape as the recesses and matching an outer circumferential surface shape of the filtration membrane modules. The guide plate comprises struts between the through holes.
An inlet center opening 712 of the distributor 205 is an inlet for feed water, scour air from the bottom and cleaning fluid. From the center opening 712 feed water, air and/or cleaning fluid is distributed into the vessel to each membrane 3 via a pattern of holes in the distributor 205. This pattern of holes in the distributor is aligned to holes in the support plate 217. There may be two or more different inlets for scour air. The scour air may be injected from bottom of the vessel 1, but there may also be the possibility to inject scour air through air scour plates, e.g. a top scouring plate 702 and a bottom scouring plate 703 which may be fed by scouring air via air channels 701. The top air scouring plate 702 may have internal air channels. Air holes 704 perpendicular to the membrane elements 3 will press scouring air into the core of membrane element 3 and improve the scouring effect of the air during backwash operation. This air scouring plate 702 will also force air from bottom support plate 217 to pass through by entering into the center of membrane element 3. The air channels 701 are provided from a bottom or an upper distribution plate to the air scouring plate 702. Furthermore there may also be channels 700 for return of cleaning fluid from top to bottom.
In
As shown in
The recesses 220 are arranged such that when the membrane elements 3 are inserted the grooves are wide enough for water and air to pass around into the vessel 1 so that fluid can flow around the membranes 3 during normal operation. When the membranes 3 are backwashed and the system is drained the drain water goes back the same way feed water enter through the support plate 217 and is collected in the distributor 205 for returning through the central opening 712 and an attached pipe to drain.
The groove 900 in the support plate 217, called air scour chamber, is filled with air from a separate inlet pipe during the phase of air scouring. From the bottom groove 900 air is directed into the air scour plate 702 through the channels 701 as air scour pipes. The air scour plate 702 has internal channels in the wall of each punching 120 which guide air jets via air holes 703 perpendicular to all membrane elements 3.
Cleaning fluid enters through the center opening 712, flows through the support plate 217, via air channel 701 and the air scouring plate 702 up to the top of return pipes 700 and back into a return chamber 901. Cleaning fluid is collected in the return chamber 901 and returns via a cleaning outlet 710 through a return nozzle 902.
The distributor 205 can also have bolting holes 904, as shown in
Regarding the top portion of the vessel 1, as further shown in
Cleaning fluid may return from the top portion 910 via return pipes 700. Outlet channels 911 for scouring air enter from underneath the guide plate 114 through the retaining plate 109, collector 105 and top dished endcap 104. The retaining plate 109 covers all membranes 3 and prevents buoyancy to lift the membrane elements 3.
The area between the guide plate 114 and the retaining plate 109 is filled with permeate. The gasket 110 on the rim of the guide plate 114 together with the gaskets 110 around each membrane element 3 is provided for separation between feed and permeate water. The pressure difference within the vessel 1 is across the guide plate 114.
The pattern of ribs 602 and cavity in the top collector 105 collect permeate water from the retaining plate 109 and give support to the retaining plate 109 and thereby also the guide plate 114 during filtration. During back wash the pressurized air drive permeate water remaining in the collector 105 back into the vessels 1 lower part.
The holes 120 in the guide plate 114 guides the membrane elements 3 during installation and give radial sealing for O-rings on each membrane element 3. In addition a groove inside the upper part of the hole 120 gives support to a C-clip mounted on the membrane element 3. The C-clip keeps the membrane element 3 in a fixed vertical position. The support plate 217 may not carry any weight from the membrane elements 3.
A vessel 1 as defined in
According to the mentioned embodiments according to
This new design reduces the footprint and weight of the system and improves the user operability and maintainability compared to existing known systems. The design may reduce the number of internal parts significantly and hence may limit the probability for leakages.
As an example for a reduced footprint, the footprint of a filtration system with 240 membrane modules may be reduced by approximately 70%.
Some embodiments may make use of composite material which reduces weight, increases strength, eliminates corrosion and provides a flexible, non-rigid design. This flexible design eliminates potential for vessel expansion during hazardous exposures, i.e. the use of composite materials eliminates potential for vessel expansion failure and potential hazardous gas release in case of fire.
It is advantageous that existing ultrafiltration standard hollow fibre membrane modules designed for onshore applications can be used. Furthermore the pressure rating of the pressure vessels can be increased from 6*105 Pa to 15*105 Pa ( over atmospheric pressure) for offshore use.
The internal design may be made such that it allows for easy inspection and removal/replacement of single elements. The top end cap with a common locking plate—i.e. the retaining plate and/or the support plate—for membrane sealing can easily be removed enabling access to all single membrane modules in one go. Then each individual membrane seal can be removed enabling operator to remove that specific element without breaking the seals for the other membrane elements. Still, no individual internal parts for each element are required except for the seal itself. The disclosed sealing system is characterized by a retaining plate (locking the seals) and a support plate (seating the seals and guiding the membranes).
The modular design allows easy fabrication hence minimizing the fabrication time.
Integrated backwashing design for multi elements may also be provided. Particularly multi membrane air scouring and backwashing may be allowed simultaneously.
Further advantages of certain embodiments may include:
1) The feed inlet distribution may be combined with the air distribution reducing the number of vessel connections external to the vessel. No internal connection parts for each individual membrane module are required.
2) Hexagonal distribution pattern of the membrane elements increases packing density thus reducing vessel diameter.
3) Unlimited pressure rating may be possible with respect to design as the distribution and collection systems have been made internal and integrated in the pressure vessel design. Only limiting factors may possibly be the choice of material and sizing of wall thickness.
4) An improved maintenance time and easy inspection and removal of single membrane modules due to internal design.
5) Weight reduction, increased strength, corrosion eliminated, and flexible design due to possible use of carbon fibre and/or epoxy materials.
6) Vessel expansion/failure may be eliminated with use of composite materials. Potential hazardous gas release in case of fire may be also eliminated with use of composite materials.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10168697.0 | Jul 2010 | EP | regional |
This application is a U.S. National Stage Application of International Application No. PCT/EP2011061406 filed Jul. 6, 2011, which designates the United States of America, and claims priority to EP Patent Application No. 10168697.0 filed Jul. 7, 2010 The contents of which are hereby incorporated by reference in their entirety.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2011/061406 | 7/6/2011 | WO | 00 | 3/22/2013 |
