瑞典专利SE0950137A1 A multifunctional module

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专利摘要:
The present invention relates to a multifunctional module comprising one or more devices selected from; the group consisting of reactor units, filter units, membrane units, reactor-separator units, clarifier units, purifier units, extractor units, and mixing units. rotator together with the body. The organ rotates about an axis which causes the unit to work with centrifugal force; One or more chambers for fluid rotating together with the rotating member. The present invention provides devices that can be used in a rotating multifunctional module, and the use of a rotating multifunctional module. No.2242 S. 24
公开号:SE0950137A1
申请号:SE0950137
申请日:2009-03-10
公开日:2010-09-11
发明作者:Tommy Noren；Barry Johnson；Kasper Hoeglund
申请人:Alfa Laval Corp Ab；
IPC主号:

专利说明:

Has a member which rotates about an axis. The units in the multifunctional module can be connected in parallel or in series or both and to each other. The module can have one or ﬂ your inlets and one or ﬂ your outlets, and the module can also include a foundation for the units.
The foundation can have connections between the units integrated in the foundation, or connections between the units can be made between the units over the foundation. A lid or hood may cover the foundation and units and leave the inlets and outlets connected to connections for supplying and collecting end product on the outside of the lid or hood.
The unit operations performed in the module can be a combination of mixing, combining, reaction, separation etc. or the module can be a combination of units within the same unit operation, the module can thus for example separate different fractions of a mixture within a module having different separation units . A module according to the invention can as an alternative carry out single-stage or first-stage synthesis, i.e. be a combination of reactor units and separation units, etc. The rotating multifunctional module according to the invention comprises units that work in different ways, e.g. a reactor unit in the module enables contact between reactants so that a reaction can take place. An alter unit is a unit where an alter is one of the components, a membrane unit is a similar unit. In an alter unit or a membrane unit, particles or molecules are separated from ider uids. In a reactor-separator unit, reactions take place as well as separation of the product mixture. A purification unit is a unit where a liquid is clarified from particles or sludge, and a purifier unit, for example, purifies an id uid. An extractor unit facilitates extraction of, for example, substances from one ﬂ uid to another or the extraction can take place to or from a gas or to or from a liquid. A contact unit can be a packed bed or an unidentified bed. A mixing unit can, for example, mix two immiscible liquids to produce, for example, an emulsion, but other kinds of mixing can also be carried out in a mixing unit.
The units in the multifunctional module according to the invention may have at least one member having a surface, which surface rotates with the member. The said surface is the surface on which the process takes place, therefore the surface is called the process surface or only the surface. The processes can be mixing, reaction, separation, etc. The rotating member can be of any kind that rotates around an axis, such a member is for example a flat or flat disc called here T-disc. Another example is a cone-shaped disc, which is a cone with an open end facing upwards, hereinafter referred to as a Y-disc. Yet another type of rotating member has a more complicated structure with extended surfaces, with two horizontal surfaces separated by a number of walls surrounding the axis of rotation and which walls diverging from a horizontal surface to the opposite horizontal surface, this kind of member is hereinafter referred to as Z-disc. Yet another kind of organ is the delta disc which has a shape like an upside down cone with the narrow end facing upwards, this kind of organ is hereinafter called the A-disc. The rotating member according to the invention can thus be selected from the group consisting of T-discs, Y-discs, Z-discs and A-discs. The active surface of the rotating member may be surfaces on the outside of the T-discs, the Y-discs, the Z-discs, or the A-discs, or the active surface may be integrated with the member in the form of one or more channels. The means which rotates about an axis during operation and works with centrifugal force, thus creating transport of products, mixing of products, separation of components, etc., and can be performed on a number of levels and with connections within the disks or between the disks.
The centrifugal force causes heavier components to be transported out from the center of the member to the mantle surface or to only a part of the distance to the edge of the member. The number of revolutions with which the body rotates can be adjusted to optimize the predetermined mode of operation. One or more of your chambers rotate together with the rotating member and collect material from the member. The chambers may surround the mantle surface of the organ, or the chamber may be located below the mantle surface of the organ, or the chamber may be located above the mantle surface of the organ, or the chamber may be located at the mantle surface of the organ. In the chamber, a stator can be arranged opposite the rotating member according to an alternative of the invention. The chambers may be shell chambers having one or more shell members, which may be shell discs, shell tubes or shell passages or combinations thereof. The shell passages may be closed or open, and the shell means are arranged relative to the chambers so as to ﬁ n a surface of the ﬂ uids in the chamber at a certain predetermined level in the rotating shell chamber.
The shell means can be connected to the shell chambers from below, which makes it possible to lead out ﬂ uider with the help of gravity. The supply of ﬂ uider to the channels in the disc can also be arranged jointly in a shell tube, such an arrangement makes it possible to supply ﬂ uider at different levels in a disc which has lager your layers of channels in the disc. A shell pipe for supply consists of two pipes, one for supplying ﬂ uider to the channel and one for placing the surface of ﬂ uiden at a predetermined level at an inlet part of the disc.
One or more of the shell discs may be centered on the axis of the rotating member and lead out ﬂides which are close to the center of the surface or the shell disc may have a radius corresponding to the rotating member, and the shell disc may be a stator arranged opposite the rotating member. The shell disks can have any diameter depending on which fraction of the ﬂ uids are to be led out of the rotating disk.
The fluids can thus be pumped up through the shaft of the stator or by a rotating member of the shell discs. The module according to the present invention may also comprise one or more static separators connected to the units having rotating means. The static separators can be connected in parallel with the units, or in series, or both, to the units in the module.
According to this alternative, the module can consist of one or enheter your units having rotating members and one or ﬂ your static separators. The static separators can be selected from clarification tanks, cyclones, coalescing units, contact units, filters, membranes, adsorbent means. According to a further alternative, one or ﬂ your high speed separators, or one or ﬂ your decanter centrifuges, or combinations thereof, may be connected to the units in parallel, or in series, or both and, to the units in the module. reactor unit or a present invention also relates to a mixing unit. The reactor unit or mixing unit comprises at least one rotating member having a surface, which surface rotates with the member, and the member is selected from the group consisting of T-disks. Y-discs Z-discs, and A-discs. The rotating member of the unit rotates about an axis which causes the unit to operate by centrifugal force. The reactor unit or mixing unit also includes one or ﬂ inlets for ﬂ uider over the body at the center of the disk at the axis or within a radial distance from the center of the disk, so that the ider uids mix, or react or are transported, or combinations thereof of the radial velocity to the body surface. The unit further includes one or more chambers for rotating together with the member. The chambers may surround the mantle surface of the organ, or the chambers may be located below the mantle surface of the organ, or the chambers may be located above the mantle surface of the organ, or the chambers may be located at the mantle surface of the organ. As an alternative, the reactor unit or mixing unit may also comprise one or more inlets for ﬂ uider at the shaft at the center of the disk leading ﬂ uider into channels inside the rotating member. The channels inside the disc go from the center to the circumference in the radial direction and lead the incoming ﬂ uider to the mantle surface. This single or your channels can communicate with each other at one or your connection points so that two or your uides can mix and / or react with each other. As an alternative, the channels can be arranged at ﬂ your levels in the disc. Channels at different levels can be connected so that two or ﬂ era ﬂ uids can mix and / or react with each other. As an alternative, two or ﬂ your channels at the same level can be connected so that two or more ﬂ uids mix and / or react with each other.
The present invention further relates to an alternative unit or membrane unit comprising at least one member having a surface, which surface rotates together with the member, and the member is selected from the group consisting of T-discs, Y-discs, Z-discs or A-discs. The means rotates about an axis which causes the unit to operate under the influence of the centrifugal force, and the means comprises at least two chambers separated by a diaphragm or a lamp or both. One or more inlets for ﬂuides are connected across the disc surface at the shaft at the center of the disc or at a radial distance from the center, and some of the ﬂuides pass through the filter or through the diaphragm and are transported by the radial velocity to the mantle surface.
The filter unit or membrane unit further comprises one or more chambers for rotating with the member. The chambers can surround the mantle surface of the organ, or the chambers can be found below the mantle surface of the organ, or the chambers can be found above the mantle surface of the organ or the chambers can be found at the mantle surface of the organ.
As an alternative to the above-mentioned för uider chambers, the chambers 10 may be shell chambers having one or ﬂ your shell disks, shell tubes or shell passages, or combinations thereof, arranged at the surface of the ﬂ uids within one or ﬂ your shell chambers. The shell passage can be closed or open. The shell plates, tubes or passages may be arranged to lead ﬂ outwards from the chambers, into one or ﬂ your outlets in radial direction from the body, into one or ﬂ your outlets below the body, or into one or ﬂ your outlets over the body, or through the shaft upwards or downward, or combinations thereof.
The present invention also relates to a reactor-separator unit comprising at least one member having a surface, which surface rotates with the member, and the member is selected from the group consisting of T-discs, Y-discs, Z-discs, and A-discs. The member of the reactor-separator unit rotates about an axis which causes the unit to operate by centrifugal force. The unit may also include one or more inlets for ider uider over the discs, but the inlets may also be found below the disc. The reactor-separator unit comprises one or two shell chambers having shell tubes which shell chambers rotate with the members. The shell tubes are connected to chambers as they. Nier the chambers. The surface of the i uids in the rotating members and the co-rotating chambers are arranged on the same axis as a centrifugal separator, which may be of any kind and be arranged above, below or around the rotating members and the co-rotating chambers.
The rotating member and the co-rotating chamber may be centered on the same axis as a centrifugal ball having a stack of insert plates inside the centrifugal rotor. The centrifugal rotor, the stack of insert plates, can be centered below or above the member on the same axis.
The stack of insert plates and the centrifugal rotor rotate together with the body and the shell chambers. At least one of the shell tubes or shell passages may be connected between at least one of the shell chambers and the centrifugal rotor leading ﬂ uider into the centrifugal rotor. The present invention further relates to an extractor unit comprising at least one member having a surface, which surface rotates with the member, and the member is selected from a group consisting of T-discs, Y-discs, Z-discs, and A-discs. The body of the extractor rotates about an axis which causes the unit to work with centrifugal force. The extractor unit comprises one or two shaft chambers which have shell tubes which shaft chambers rotate together with the members. Inlets for liquids and gases, or liquids, are arranged so that the liquids flow with or against the flow through the unit. Alternatively, a centrifugal rotor may have a centrifugal ball and a stack of insert plates on the same axis as the rotating member and the co-rotating chambers. The centrifugal rotor can thus surround the rotating member, be located on top of the rotating member or below. The insert plates may thus surround the rotating member and the co-rotating chamber, or the insert plates may be below or above the rotating member. A shell tube or shell disk can transport ﬂ uider to the centrifuge ball from the rotating member having a co-rotating chamber.
Alternatively, the units mentioned above may have a plate or housing centered on the shaft of the member attached to cover the surface of the member or attached to the same extent to the surface of the member and leave a gap between the plate or housing and the rotating member. The plate or housing may be stationary or may rotate at a different number of turns than the rotating member, and the plate or housing may rotate together with the rotating member or rotate counterclockwise towards the rotating member. The housing or plate can be heat exchanged with heat exchanging ﬂ uider. As a further alternative, a shell disk may transport ﬂider through the outlet in the shaft of the stationary plate or stationary housing, or a pump may be connected to the inlet for pumping ﬂider out through the outlets in the shaft.
As a further alternative to the above-mentioned means according to the invention, the rotating means may be covered by a protection, and the protection may be provided with inlets and outlets for ider uids, such as liquid ider uids, sols, gases, id uidized particles etc. The protection may be sealed to contain a gaseous medium. The units can be hermetically sealed. Gas-tight gaskets can seal the parts and the rotating shaft at transition points between the different parts.
A further alternative to the present invention is that at least one surface of the members or at least a part of the surface of the members may be coated with one or more catalysts.
In the following, the present invention will be described with the aid of urer gures. Figures 1 to 15 are only examples of the invention that explain this and are not intended to limit the scope of the invention.
Brief description of the structure Figure 1 shows a rotating module according to the structure.
Figure 2 shows a T-disc according to the invention.
Figure 3 shows a T-disc with a stator according to the invention.
Figure 4 shows an inlet to a T-disc which has channels according to the invention.
Figure 5 shows another view of a T-disc having channels.
Figure 6 shows yet another view of a T-disc having channels.
Figure 7 shows a membrane or filter unit according to the invention.
Figure 8 shows an A-disc inside a centrifugal separator according to the invention. Figure 9 shows another A-disc inside a centrifugal separator according to the invention.
Figure 10 shows an A-disk unit according to the invention.
Figure 11 shows a hermetic unit according to the invention.
Figure 12 shows another hermetic unit according to the invention.
Figure 13 shows a Z-disc according to the invention.
Figure 14 shows a Y-disc according to the invention.
Figure 15 shows a detailed drawing of a shell tube located under a T-disc according to the invention.
Detailed description of the durations Figure 1 shows a multifunctional module that has four units 1, the units can have different sizes, different kinds of processes etc. In Fig. 1 the units are located under a hood 2 on a foundation 3. A supply pipe 4 and a product pipe 5 out from the module is displayed in the clock which illustrates that the process module is continuous. How the units are configured in the modules depends on space, what kind of processes and the sequence of processes, the units can be connected in series and the units can thus be arranged in a row or the units can be placed in a square shown in the clock. A combination of units connected in series and in parallel with each other is an alternative to the module shown in Figure 1, another may be that all the units can be connected in parallel. All units in a module can be "rotating" or have parts that rotate around an axis, or some of the units can be stationary units.
Figure 2 shows two equipment according to the invention, Figure 2 shows two different arrangements illustrated in Figure one on each side of the axis 6 A + B.
A and B represent two different types of equipment, but A and B also represent two different supply inlets for reactants which will react with each other and form a product C. On the A-side of the equipment, a stator 7 is arranged above a T-disk 8. The stator 7 and the T-disk 8 are arranged so that a gap is formed between the stator 7 and the T-disk 8 to enable a space for reactions. The movement of the fluid is created by the stator 7 and the disc 8 can enable better movement to create better reactions between different components in the inlet fates. There is no stator on side B of the equipment and the reaction surface is open. Supply of reactants A and B is at an inlet at the center of the T-disc 8, but the reactants can also be supplied within a part of a radial distance from the center, the reactants begin to react and mix and form a ﬁ lm or a layer on the surface of the disc. Reactants and products are transported by the centrifugal force to the edge of the disc where a chamber 9 collects the material. The number of rotations with which the disk rotates depends on various properties such as the viscosity of the reaction mixture, reaction time, etc.
The chamber 9 rotates together with the T-disc 8. In Fig. 2 the disc is represented by a disc attached to a shaft 10, but according to the invention it is also included that the disc 8 is not attached to the shaft, the disc is instead mounted on the chamber 9 which chamber is connected to the driving force of the engine according to this option, this option is not shown in the figure. A shell tube 11 is connected from below with the disc to the chamber 9 for transporting the product mixture C out of the chamber 9. According to this placement of the shell tube 11, it is possible to transport C by gravity from the chamber 9. The dynamic pressure forces the ut uids out of the chamber.
Figure 3 shows a unit having a T-disc with a co-rotating chamber for products. The process mixture is transported by the shell disk 12 from the co-rotating chamber according to this alternative of the invention, and the process mixture is then pumped out through the stator shaft 13. A housing 14 closes the disk from the environment so that gas can be supplied.
Figure 3 also shows how heat is transported to and from the units through heat exchangers. The heat exchanging ider uids are transported in channels 15 through the rotating shaft 16 from below opposite to the process side of the disk 8. According to this alternative, the disk 8 is not attached to the rotating shaft 16 but the disk 8 is instead mounted to the co-rotating chamber. A stator 7, which may be a shell disk but not necessarily, is attached to the stator shaft 13.
Figures 4, 5 and 6 show a T-disc having integrated process channels 17. Inlet 18 supplies process channels to the channels 17. In Figure 4 a shell tube 19 secures the level of a fate path 20 of process channels connected to the channels 17. Figure 6 shows the outlet tube 21 which leads process products out of the co-rotating chambers inside the disc, which is not shown in detail in Figure 6.
Figure 7 shows an alter or a membrane unit according to the invention.
Process ﬂ uider is led into the chamber 22 where an alter 23 or a membrane 23 divides the chamber 22 into two parts. The process liquids are separated by the filter or membrane and both concentrate and filtrate, or permeate transported by the centrifugal force to be collected in co-rotating chambers, are not shown in detail in Figure 7. A shell tube 24 transports concentrate from the co-rotating chamber intended to collect concentrate through a stator shaft 13. The filtrate and permeate are transported by a shell tube 24 up through the stator shaft 13. A shell tube or shell disk will pump both concentrate and atlrate / permeate through the stator shaft.
Shell discs can replace one or both shell tubes 24 or 25 according to an alternative.
Figure 8 shows an A-disc 26 inside a centrifugal ball 27 according to the invention.
This option is without an extractor. Process n inlet 28s are centered on a stator shaft to supply process ider uider into a space between the A-disc 26 and rotor body 29. The process ﬂ uids react and the product mixture is transported on the surface 26 of the A-disc 26 to be collected in a co-rotating chamber Which according to this embodiment is a centrifugal ball 27. In the centifugal ball there is a stack of insert plates 31. The insert plates 31 form an extended surface for the separation equipment.
The product mixture is separated and the different fractions of the product mixture are pumped out of the centrifuge ball by one or more of the shell discs 32. Heat exchangers are transported from inlet 33a to the A-disc 26 and thus conduct heat to and from the process reactions.
The heat exchangers are collected in the chamber 34 and transported out of the shell tube 35.
Figure 9 shows an alternative A-disc with an extractor. According to this alternative, gas can be supplied through an inlet or outlet through the shaft 33c to or out of the space 36 between the A-disc 26 and the rotor body 29 and be connected to outlet or inlet 33b and the unit will function as an extractor.
Figure 10 shows an A-disk having a shell tube 37 or a shell disk 37 at the bottom of the disk transporting the process utides out of the chamber 38. The fluids are transported up through the stator shaft 39. Alternatively, a shell disk may transport ider uider from the chamber 38 through the rotating shaft. shaft 40, is not shown in Figure 10. The supply inlets 41 supply process uides into the A-disk and the uides are transported by the centrifugal force down to the chamber 38 where the uides are collected before further transport.
Figure 11 shows a hermetic unit having a T-disc 44. According to this version of the present invention, process ﬂ is applied up the axis of rotation 43 to through the upper surface of the stator 42.
The process kommer uids will be pumped down from the surface of the T-disc 44 through the rotating shaft 43 from the chamber. Heat exchangers ﬂ uider are transported up and down through the rotation shaft 43 for heat exchange to or from the T-disc 44. A housing 45 seals the T-disc from the surroundings. Figure 12 also shows a hermetic T-disc assembly. According to this alternative, process leads are supplied through the inlet 46 into the housing 45. The process leads are led out through the outlet 47 in the housing. A heat exchanger 48 is centered on the rotating shaft to heat exchange the heat exchangers within them to and from the T-disc.
Figure 13 shows a Z-plate having two horizontal surfaces 49 and 50 separated by a number of walls 51 and 52. Walls 51 and 52 surround the axis of rotation and extend diverging from a horizontal surface towards an opposite horizontal surface.
Figure 14 shows a Y-disc 53 according to the invention. The process ﬂ uids are supplied through inlet 54 from above the Y-disc. The process ﬂ uids are released at the bottom surface of the Y-disc. By the centrifugal force, the ﬂ guides are forced up onto the surface of the Y-disc and collect in the chamber 55. A shell disc 56 or a shell tube 56 transports the ﬂ guides from the chamber 55. The Y-disc is cold or heated by heat exchangers ﬂ uides, which are let in or out through the shaft 57 in to a space 58 between the Y-disc and the rotor 59.
Figure 15 shows a more detailed view of a unit having a shell tube 60 located below a T-disc for transporting fluids out of a shell chamber 62, there may be more than one shell tube 60 arranged below the disc. This figure shows how the shell tube 60 defines the surface 63 at a predetermined level depending on the position of the shell tube 60 in the chamber 62. In this figure, the T-disc 61 is mounted on the rotor body 64. The figure also shows that the shell chamber 62 is attached to the rotor body 64 with a or ﬂ your bolts 65.
A stator 66, according to this alternative, is placed over the T-disc 61 and leaves a gap 67 for ﬂ guides, which ﬂ guides are supplied through the inlet 68 in the stator shaft. According to another alternative, which is not shown in Figure 15, the stator may be superfluous and leave the rotating surface open below the protective shell 69. According to another alternative, not shown in Figure 15, the stator may be a shell disk, but then the shell tube may 60 may be unnecessary in some applications, but not necessarily. If there is a shell disc, the T-disc 61 is mounted in such a way that the chamber 62 will cover the T-disc 61 and the peel disc. According to this alternative, the från uids from the chamber 62 will be pumped up through the protective cover 69 of the shell disk. Figure 15 shows inlets 70a and outlets 70b for heat exchangers ider uider, which are arranged in the rotating shaft 71 and allow heat exchanger fluids to be pumped to the channels 72 below the T-disc 61 to heat or cool the disc. The design of the disc is, according to this alternative, shown in Figure 15 a T-disc 61 in the form of a plate mounted on a rotor body 64, but according to other alternatives the shape of the disc may be a T-disc, a Y-disc, a Z-disc disc or an A-disc. The shape of the disc depends on the function of the unit and Figure 15 shows a T-disc, but the size is not limited to this version. When a T-disc, Y-disc, Z-disc or an A-disc is used, all these kinds of discs are mounted on a rotor body 64 and not on a rotating shaft, of course these discs can be mounted on a rotating shaft but not according to the alternatives in ﬁ gur 15. The Y-disc can therefore be a cone-shaped bowl with the narrower end facing downwards, the A-disc can also have a cone-shaped but in this alternative the narrower ends are turned upwards. The Z-disc can be turned in both of these ways because the disc is symmetrical. The shell chamber 62 is mounted together with the selected disk on the rotor body 64 which covers the disk and the rotor body according to these alternatives of the invention. Depending on the disk used, the shell chamber 62 may have different sizes to cover both the disk and the rotor body. The housing 69 may have one or more of its inlets and / or one or two of its outlets, none of which is shown in Figure 15 except for the inlet inlet 68 which is an alternative. As another alternative, not shown in Figure 15, a centrifugal rotor may have a centrifugal ball and a stack of insert plates may be centered on the same axis as the disk and shell chamber 62. The centrifugal rotor may surround the disk, or be located above or below the disk. the insert plates may thus surround the disc, or the insert plates may be above or below the disc 61. A shell disc or a disc may transport ﬂ uider into the centrifuge ball from the chamber 62 when the centrifuge ball ﬁ is below the disc 61. When the centrifuge ball ﬁ ns over the disc 61 pumps the disc disc 62 from the disc disc. in the centrifuge ball. According to the alternatives to the invention presented in Figure 15, the selection of the disc 61 may be possible, which enables the unit to be assembled depending on the desired purpose of using the unit. The device is thus very flexible and possible to change.

权利要求:
Claims (6)
[1]
A multifunctional module comprising one or more units selected from the group consisting of reactor units, filter units, membrane units, reactor-separator units, clarification units, purification units, extraction units, and mixing units, where the units are connected in parallel. or in series or both, and each unit has at least one rotating member having an effective surface, said operative surface rotating with the member, said member rotating about an axis which causes the unit to operate by centrifugal force, and wherein the unit also includes one or more chambers for ﬂ uider rotating together with the rotating member.
[2]
A multifunctional module according to claim 1, wherein the module also comprises one or ﬂ your static separators, one or ﬂ your high speed separators, or one or ﬂ your decanter centrifuges, contact units, or combinations thereof connected to the units in parallel, or in series, or both and with the devices.
[3]
A multifunctional module according to claim 1 or 2, wherein the rotating member of one or more units is selected from the group consisting of T-discs, Y-discs, Z-discs and A-discs, wherein the active surface is integrated with the member so that the surface is above or below the T-discs, the Y-discs, the Z-discs, and the A-discs or the active surface so that the surface ﬁ ns inside the body in the form of one or ﬂ your channels.
[4]
A multifunctional module according to claim 1, 2 or 3, wherein one or ﬂ your chambers for ﬂ uides rotating together with the rotating member are shell chambers having one or ﬂ your shell members, and the shell chamber 10 surrounds the shell surface of the member, or the shell chamber Appears below the mantle surface of the organ, or the shell chamber appears above the mantle surface of the organ, or the shell chamber appears at the mantle surface of the organ.
[5]
A reactor unit or a mixing unit comprising at least one means having an active surface, which active surface rotates together with the means, and the means is selected from the group consisting of T-plates, Y-plates, Z-plates, and A-plates, and the means rotates about an axis which causes the unit to operate by centrifugal force, the reactor unit or mixing unit also comprising one or ﬂ inlets for ﬂ uider over the means at the center of the disk at the axis or within a radial distance from the center of the disk so that the uids are mixed, or reacted or transported , or combinations thereof of the radial velocity of the mantle surface of the disc, and wherein the unit also includes one or more chambers for rotating together with the member, and the chamber surrounds the mantle surface of the member, or the chamber is located above or below the mantle surface of the member, or the chamber is at the member mantelyta.
[6]
A reactor unit or a mixing unit comprises at least one means having an active surface, which active surface rotates together with the means, and the means is selected from the group comprising T-plates, Y-plates, Z-plates and A-plates, the means rotating around a shaft which causes the unit to operate by centrifugal force, where the reactor unit or mixing unit also includes one or ﬂ inlets at the center of the disk at the shaft, where the body has channels within the disk extending from the center to the mantle surface in the radial direction leading incoming ﬂ uider to the mantle surface and one or your channels can communicate with each other, and chambers surround the mantle surface of the organ, or the chambers form below the mantle surface of the organ, or the chambers form above the mantle surface of the organ, or the chambers form at the mantle surface of the organ. An alternative unit or a membrane unit comprises at least one member having an active surface, which active surface rotates together with the member, and the member is selected from the group consisting of T-discs, Y-discs, Z-discs , and A-discs, wherein the means rotates about an axis which causes the unit to operate by centrifugal force, the means comprising at least two compartments divided by a diaphragm or an ﬁlter or both and, one or ﬂ inlets for ﬂ uider over the surface of the disc at the center of the disc at the shaft or at a radial distance from the center, so that parts of the iderides pass through the filter or through the membrane and are transported by the radial velocity to the mantle surface, the unit also comprises one or ﬂ chambers for ﬂides rotating together with the member, and the chamber surrounds the mantle surface of the member, or the chamber is formed above the mantle surface of the organ or the chamber is formed below the mantle surface of the organ, or the chamber is formed at the mantle surface of the organ. A reactor-separator unit comprising at least one means having an active surface, said active surface rotating together with the means, and the means is selected from the group consisting of T-plates, Y-plates, Z-plates and A-plates, the means rotating around a shaft which causes the unit to operate by centrifugal force, the unit also comprising one or ﬂ inlets for ﬂ uider over the disks, the unit also comprises one or more shell chambers for ﬂ uides rotating together with the unit and having one or ﬂ your shell tubes connected to the surface of the fluids in the shell chambers, and the unit also includes a stack of insert plates within the centrifugal rotor below the member having the same axis as the member, said stack of insert plates and centrifugal rotor rotating together with the member and the shell chambers, at least one of the shell tubes connected between at least one of the shell chamber roots and centrifuge. An extractor unit comprising at least one member having an active surface, which active surface rotates together with the member, and the member is selected from the group consisting of T-discs, Y-discs, Z-discs, and A discs, the means rotating about an axis which causes the means to operate by centrifugal force, the extractor unit also comprising one or ﬂ inlets for ﬂ uides on both sides of the means causing the ider uids to ﬂ surface downstream or countercurrent through the extractor unit, the various ﬂ uids mixing, or reacting or transported, or combinations thereof by the radial velocity of the organ and transported to the mantle surface of the organ, the unit also comprising one or ﬂ your chambers for rotating with the organ, and the chamber surrounds the mantle surface of the organ, or the chamber is below the mantle surface of the organ or the chamber the mantle surface of the organ, or the chamber is located at the mantle surface of the organ. An assembly according to any one of claims 5 to 9, wherein the chambers for ﬂ uider are shell chambers having one or ﬂ your shell means arranged to ﬁ nier ﬂ uid surfaces at predetermined levels in one or ﬂ your shell chambers, and the shell means are arranged to guide the ider uids out of the chambers, in. to one or ﬂ your outlets in the radial direction from the organ, into one or ﬂ your outlets below the organ or one or ﬂ your outlets over the organ, or through the axis upwards or downwards, or combinations thereof. An assembly according to any one of claims 5 to 10, wherein a plate or casing is centered on the shaft of the member attached to cover the surface of the member or attached to have the same extent as the surface of the member and leaving a gap between the stationary plate or the stationary housing and the means, where the plate or housing and the means, where the plate or housing is stationary attached to or rotates with or against the means with a different number of rotations. An assembly according to claim 11, wherein one or more of the shell discs 10 transports genom uider through the outlet in the shaft of the stationary plate or the stationary housing, or a pump is connected to the inlet for forcing the ﬂ uider through the outlet in the shaft . A unit according to any one of claims 5 to 12, wherein the channels or chambers for heat exchange ﬂ uides are integrated with the means or under the means, which heat exchange ﬂ uids are pumped from under the means at or inside the shaft which provide heat exchange to or from the means. A unit according to claim 13, wherein the heat exchanger ﬂ uids are passed through a heat exchanger centered on the shaft below the member. A unit according to any one of claims 5 to 14, wherein the unit also comprises pumps for heat exchangers ﬂ uider, and for ﬂ uider from the chambers. A unit according to any one of claims 5 to 15, wherein the means is also covered by a casing, and the casing is provided with inlets and outlets for ﬂ uids, such as ﬂ surface ider uids, sols, gases, ﬂ uidized particles, etc. 17. A unit according to claim 16, where the unit is hermetically sealed. A unit according to any one of claims 5 to 17, wherein at least a portion of the active surface of the member is covered with a catalyst. A method of operating a multifunctional module according to any one of claims 1 to 4, wherein the ﬂids are mixed, reacted, or both in a reactor unit or a mixing unit according to claim 5 or 6, and the product ﬂ uids are then transported by at least one scale device from at least a shell chamber for a filter unit or a membrane unit according to claim 8 or for a reactor-separator unit according to claim 9, or the products are transported to a combination of separator units, filter units or membrane units. Use of a multifunctional module according to any one of claims 1 to 4, for the production of chemicals.

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同族专利:

公开号 | 公开日

SG174308A1|2011-10-28|

AU2010223131B2|2013-12-12|

CA2754717C|2015-02-03|

KR101403246B1|2014-06-02|

CN102421520A|2012-04-18|

JP2012520172A|2012-09-06|

RU2501601C2|2013-12-20|

US20120058023A1|2012-03-08|

SE536493C2|2013-12-27|

RU2011140861A|2013-04-20|

KR20110134905A|2011-12-15|

WO2010104457A3|2010-12-23|

EP2406004A2|2012-01-18|

WO2010104457A2|2010-09-16|

US8961882B2|2015-02-24|

MX2011009374A|2011-10-03|

CA2754717A1|2010-09-16|

AU2010223131A1|2011-09-29|

JP2013226553A|2013-11-07|

BRPI1008988A2|2016-03-22|

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法律状态:
2015-12-01| NUG| Patent has lapsed|

优先权:

申请号 | 申请日 | 专利标题

SE0950137A|SE536493C2|2009-03-10|2009-03-10|A module comprising a reactor unit|SE0950137A| SE536493C2|2009-03-10|2009-03-10|A module comprising a reactor unit|

MX2011009374A| MX2011009374A|2009-03-10|2010-03-04|A spinning disc multiftintional module.|

SG2011065000A| SG174308A1|2009-03-10|2010-03-04|A spinning disc multiftintional module|

JP2011553986A| JP2012520172A|2009-03-10|2010-03-04|Multi-function module|

PCT/SE2010/050250| WO2010104457A2|2009-03-10|2010-03-04|A multifunctional module|

KR1020117023583A| KR101403246B1|2009-03-10|2010-03-04|A spinning disc multiftintional module|

CN2010800212768A| CN102421520A|2009-03-10|2010-03-04|A multifunctional module|

RU2011140861/05A| RU2501601C2|2009-03-10|2010-03-04|Multifunctional module|

BRPI1008988A| BRPI1008988A2|2009-03-10|2010-03-04|multifunction module, reactor unit or mixer unit, filter unit or membrane unit, reactor-separator unit, extractor unit, process for operating a multifunctional module, and use of a multifunctional module.|

CA2754717A| CA2754717C|2009-03-10|2010-03-04|A reactor or mixer unit|

AU2010223131A| AU2010223131B2|2009-03-10|2010-03-04|A spinning disc multifunctional module|

US13/255,295| US8961882B2|2009-03-10|2010-03-04|Multifunctional module|

EP10710689A| EP2406004A2|2009-03-10|2010-03-04|A multifunctional module|

JP2013118683A| JP2013226553A|2009-03-10|2013-06-05|Multifunction module|

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