EP2305370B1 - Homogeniser and homogenising device with such a homogeniser - Google Patents
Homogeniser and homogenising device with such a homogeniser Download PDFInfo
- Publication number
- EP2305370B1 EP2305370B1 EP10011599A EP10011599A EP2305370B1 EP 2305370 B1 EP2305370 B1 EP 2305370B1 EP 10011599 A EP10011599 A EP 10011599A EP 10011599 A EP10011599 A EP 10011599A EP 2305370 B1 EP2305370 B1 EP 2305370B1
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- European Patent Office
- Prior art keywords
- rotor
- stator
- homogeniser
- homogenizer
- housing
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- 238000010008 shearing Methods 0.000 abstract description 18
- 230000000694 effects Effects 0.000 description 20
- 230000009969 flowable effect Effects 0.000 description 18
- 239000006185 dispersion Substances 0.000 description 11
- 238000000265 homogenisation Methods 0.000 description 11
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Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/21—Mixers with rotary stirring devices in fixed receptacles; Kneaders characterised by their rotating shafts
- B01F27/2123—Shafts with both stirring means and feeding or discharging means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
- B01F27/2711—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator provided with intermeshing elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
- B01F27/2714—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator the relative position of the stator and the rotor, gap in between or gap with the walls being adjustable
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71775—Feed mechanisms characterised by the means for feeding the components to the mixer using helical screws
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/41—Emulsifying
Definitions
- the invention relates to a homogenizer for the homogenization or dispersion of flowable materials, with a rotatably mounted at least one rotor, and rotatable by means of a, in particular controllable, drive rotatable shaft and with a rotor cooperating with the stator, wherein between the rotor and the stator at least one shear gap is formed.
- the invention further relates to a homogenizer for homogenizing or dispersing flowable materials, with a particular equipped with a return container with at least one branching off of the container and leading into an inlet of a homogenizer of the aforementioned type branch line.
- Such homogenizers are widely used for the homogenization or dispersion of flowable substances, such as liquid to more or less viscous substances or mixtures of substances, for example emulsions, dispersions, etc., for example in the chemical, pharmaceutical, cosmetic and food industries. It will be the homogenizers often operated together with a stirred tank, wherein the homogenizer in a outgoing from the container and optionally in this recirculating line, preferably at a level in the region of the lowest point of the container or below it, may be arranged, so that the homogenizer in addition to the agitator of the container contributes to a proper homogenization or dispersion of the product.
- the homogenizing effect is based primarily on the entry of shear forces on the flowable substances by rotation of the rotor, which cooperates with the counterpart stationary stator.
- the rotor may have one or more rotor blades, for example, in each case one arranged on both sides of the stator rotor blade, each defining a shearing gap between itself and the stator.
- generic homogenizers offer the advantage of a simpler and more cost-effective design and, in particular, a lower-wear operation.
- the rotational speed of the rotor with respect to the stationary stator can be controllable, the shear effect increasing with increasing rotational speed of the rotor.
- the conveying effect of the homogenizer increases with increasing speed of its rotor, so that the conveying effect is coupled directly to the shearing action of the homogenizer. This is usually due to the fact that due to the relative movement between the rotor and stator in the shear gap formed between the rotor and the stator, a speed-dependent negative pressure is generated, which is to be processed Suction product and push through the gap radially outward.
- the EP 1 395 354 B1 and DE 296 08 712 U1 describe a homogenizer in which the shear gap formed between the rotor and the stator is variable by axial displacement of the rotor. If at high speed of the rotor and consequent high conveying and heavy action latter are reduced, it can be increased in this way, the gap formed between the rotor and stator. However, even at maximum gap width of the rotor / stator system, the materials to be processed are still exposed to a not inconsiderable shearing action, and solid particles which are sensitive to mechanical action can not be dispersed in this way.
- EP 1 825 907 A1 and EP 1 125 625 A1 describe such a homogenizer, which in addition to the rotor comprises a further, individually rotationally driven element, which may be formed by a further rotor or by a conveyor.
- Other known from the prior Tecknik devices are in the documents DE 20/2006 008 820 U .
- the invention has the object of providing a homogenizer of the type mentioned in a simple and cost-effective way to the effect that its shearing effect can be limited to a minimum extent with continuous promotion, to him also an application for the processing of both very shear-sensitive substances as well to develop mechanical action of sensitive solid particles.
- this object is achieved in a homogenizer of the type mentioned and in a homogenizer equipped with such a homogenizer of the type mentioned in that the stator with respect to the rotor between at least a first position, in which at least an axial portion of the stator below Forming the shear gap is arranged radially adjacent to the rotor, and a second position in which the stator is arranged in the axial direction adjacent to the rotor, so that between the rotor and stator no shear gap is present, is axially displaceable.
- the inventive design makes it possible in a structurally simple manner that the shearing effect can be lowered by a constant, at least by the rotation of the rotor effected flow through the homogenizer on a comparison with the prior art unequal lesser level up to virtually zero by the flowable product is passed past the rotor displaced from the stator, the rotor / stator system is thus "bypassed".
- the stator is displaced into its second position in which it is arranged axially next to the rotor and consequently the shearing gap formed between it and the rotor in the radial direction is no longer present.
- the flowable substances are now only by the centrifugal forces caused by the rotor, possibly supported by a conveyor (see below), conveyed through the homogenizer through which no or at most very low shear forces in the product or in the - for example from a liquid or viscous matrix with herein einisperg convinced, against mechanical stress sensitive solid particles formed product mixture are registered, but nevertheless provided for a certain, very gentle mixing / homogenizing effect. If, on the other hand, stronger shear forces are to be introduced into the product, then the stator is displaced into its at least one first position, in which it is arranged at least partially radially next to the rotor and forms a shear gap between itself and the rotor.
- the homogenizer according to the invention can therefore be, on the one hand, in a "shear mode", which is usual for generic homogenizers, in which the stator is in the first position, on the other hand operate in a conventional generic homogenizers so far not possible, pure "pump mode” in which the stator is in the second position and the flowable product is conveyed through the stator only.
- the speed of the rotor preferably independently of the respective position of the stator, be variable in order to change the shearing and / or conveying action of the homogenizer can.
- stator in the second position with a certain axial distance, for example of at least 1 mm, preferably of at least 2 mm, in particular of at least 5 mm, is arranged by the rotor.
- stator abuts in the second position against a stop arranged on the side facing away from the rotor of the stator, in order to provide a structurally very simple way for a fixed predetermined second position of the stator, in which he product shear reliably prevented.
- stator is arranged in at least a first position substantially over its entire axial extent radially adjacent to the rotor, for a - as I said, optionally additionally variable by the rotational speed of the rotor - shear of the product and thus to ensure the highest possible efficiency of the homogenizer in the "shear mode".
- stator when the stator is displaceable exclusively between a (single) first position and the second position with respect to the rotor, it can of course also be provided that the stator is connected between a plurality of first positions, in which the stator is arranged in each case at least with an axial portion radially adjacent to the rotor, with respect to the rotor is displaceable.
- the shearing action which is always present in the various first positions of the stator, can be further varied by increasing or decreasing the shearing gap formed between the rotor and the stator.
- the rotor axially fixed and the stator can be arranged axially displaceable contrast.
- a conveying device in particular in the "pumping mode" (ie with the stator located in the second position) even at very low speed of the rotor and consequently very small, thereby caused centrifugal forces on the flowable materials at a very gentle mixture / homogenization, a sufficient flow rate of the product through the homogenizer.
- a conveyor can also serve entirely for the required in the "pumping mode" capacity.
- the homogenizer according to the invention is a so-called “external homogenizer” in which the rotor / stator system and optionally the conveyor are accommodated in a separate housing in which the shaft carrying the rotor is mounted ,
- the housing preferably has at least one inlet arranged upstream of the rotor / stator system, which inlet can be connected in particular to a branch line of a container, in particular equipped with an agitator.
- the housing preferably has at least one outlet arranged downstream of the rotor / stator system, which outlet can be connected in particular to a return line of the container, in particular equipped with an agitator.
- the homogenizer is in this way part of a circulation line from the (stirring) container of a homogenizer and into it, in order to ensure a very effective mixing / homogenization of the products either in the "shear mode" and / or in the "pumping mode".
- the homogenizer is connected as part of a homogenizer to the (stirring) container - the homogenized product through its outlet, for. is also supplied to further processing steps or a bottling, instead of recirculating it in the (stirring) container.
- upstream and downstream in this context always refer to the intended conveying direction of the flowable substances through the homogenizer, ie from its inlet, optionally via the conveyor and the rotor / stator system to its outlet.
- the preferably present conveying device can be arranged otherwise upstream or downstream of the rotor, wherein it is also possible in principle to provide both an upstream and downstream of the rotor arranged conveyor.
- the outlet of the homogenizer is expediently arranged radially with respect to the shaft carrying the rotor and in the axial region of the rotor / stator system, so that the mixed / homogenized product after passing through the rotor / stator system or - in the second Positioning stator - the rotor leaves the housing of the homogenizer radially.
- the rotor / stator system extends radially into the region of the inner wall of the housing.
- the homogenizer may, for example, have at least one conveying element that can be rotated coaxially with the shaft of the rotor, which may be designed, for example, in the form of a screw element of a screw conveyor and expediently extends around at least a part of the circumference of its axis of rotation.
- the conveying element preferably extends into the region of the inner wall of the housing, so that the flowable material at least not to a significant extent between the conveyor element and the inner wall of the housing can flow past the conveyor element.
- a small gap for example, be formed with a width of at most about 2 mm or at most about 1 mm, to ensure a low-wear operation of the conveyor.
- the conveyor eg at least one conveying element
- the conveyor is disposed on a narrowing of the inner side portion of the housing, wherein the term "narrowing" on the conveying direction of the flowable substances through the homogenizer refers.
- a mixing device may further be provided, the arrangement of which may be selected upstream or downstream thereof or also between the rotor / stator system and / or on the conveyor.
- the arrangement of which may be selected upstream or downstream thereof or also between the rotor / stator system and / or on the conveyor.
- the mixer can of course also in the conventional operation of the homogenizer in the "shear mode" additional homogenization / dispersion or - if the mixing device is arranged upstream of the rotor - cause some pre-homogenization.
- additional homogenization / dispersion or - if the mixing device is arranged upstream of the rotor - cause some pre-homogenization.
- such a configuration opens the homogenizer a practically suitable for any flowable materials use, they are relatively insensitive or highly sensitive to shear forces or against mechanical stress.
- the mixing device may preferably have at least one or in particular a plurality of mixing vanes which can be set into rotation coaxially with the axis of rotation of the rotor and which advantageously extend (only) around part of the circumference of its axis of rotation.
- a plurality of mixing vanes may preferably be arranged with radial and / or axial distance from each other, so that a uniform, gentle mixing or homogenization of the product over the entire cross-section of the homogenizer is possible.
- the mixing blade (s) of the mixing device can be arranged obliquely with respect to its axis of rotation, as a result of which the mixing or homogenizing effect can be improved and optionally an additional conveying effect can be induced;
- the mixing blades can have, for example, an approximately propeller-like shape.
- the mixing blade (s) may be perforated to provide a further improved mixing or homogenizing effect thereby allowing a (small) flow of material through the mixing blades.
- the mixing device can of course also have any differently configured mixing elements as an alternative or in addition to such mixing blades.
- mixing rods for example at least partially in the radial direction extending mixing rods are mentioned, which may for example be fixed to the axis of rotation of the mixing device and optionally with stationary stationary on the inner wall of the housing of the homogenizer with axial offset thereto arranged stationary, for example, also rod-shaped elements can cooperate ,
- the rotor and the conveyor and / or the mixing device can be set in rotation, in particular by means of one and the same, preferably controllable, drive, for example, sit on one and the same shaft, which passes through the homogenizer in the axial direction.
- the rotor may be decoupled from the drive in order to be able to convey the product, if necessary, with rotor at rest completely free of shear induced by the rotor through the homogenizer.
- the same can apply to the mixing device, provided that e.g. it is desirable to promote the flowable materials with a stationary rotor and stationary mixing device only by means of the conveyor through the homogenizer to mix them slowly and gently or homogenize.
- the rotor on the other hand, the conveyor and possibly also the mixing device, in the latter case preferably the conveyor together with the mixing device, of course, be driven independently.
- the rotor and the stator may be substantially in the form of a cylinder jacket having circumferentially distributed radial openings exposed therein, with the shear gap formed between the rotor and the stator in a first position.
- the rotor may, of course, comprise one or more rotor blades, such as two rotor blades, one of which is disposed radially inward and radially outward of the stator, so that in a first rotor Position of the stator two shear gaps are formed, wherein the individual rotor blades may in turn be driven together or separately from each other or may be individually or jointly decoupled from a respective or common drive.
- the radial openings of the rotor may preferably have a different shape and / or size than the openings of the stator.
- stator can basically also be displaced manually relative to the rotor
- an advantageous embodiment provides that an actuator is provided for displacing the stator with respect to the rotor.
- actuators for displacing the stator with respect to the rotor.
- linear actuators actuators such as hydraulically, pneumatically or hydropneumatically actuated piston / cylinder units, mechanically or equally fluidly actuated push rods, racks, screw thread, etc.
- the actuator can in each case preferably with rotating Rotor be actuated.
- the actuator is fixed to a cover of the housing of the homogenizer frontally closing, the cover with the actuator in particular from the housing of the homogenizer and removable against a provided with an end inlet opening for the task of an additional substance component lid can be interchangeable.
- the latter embodiment opens up a further application to the homogenizer according to the invention, namely the dispersing of a further substance component via the additional inlet into the flowable substance, wherein the additional substance component is in particular powdery or particulate can be.
- the additional substance component can be easily sucked in and dispersed into the substance, whereby lumping is avoided even in the case of very fine particulate matter components, because the substance components in the region of the homogenizer with very high turbulence, ie in the area of the rotor / stator system.
- the actuator can be removed in particular together with the stator axially displaceable thereon, wherein on the provided with a frontal inlet opening a stator can be fixed, of which in the mounting position of the lid at least an axial section to form the shear gap is arranged radially adjacent to the rotor, so that during assembly of the cover provided with the additional inlet, a stator is automatically arranged in a first position and consequently immediately act on the sucked further material component very high shear forces to a homogeneous Eindisperg réelle same, optionally with mechanical comminution to provide.
- the cover can of course not be equipped with a stator, or the stator can in particular be fastened detachably to the cover provided with the additional inlet in order to be able to do so to be able to remove or put on.
- the latter can be done with respect to a simple and quick installation, preferably by means of a quick release, such as a latching connection.
- the housing e.g. at the inlet opposite side of the rotor / stator system or on the side facing the same, at least one second inlet for the task of an additional substance component, wherein such a second outlet should be suitably closed by means of a shut-off.
- the stator between its first and second position when opening the obturator on the occasion of a desired dispersing a further material component in turn for a high shear (with the located in a first position stator) or for a very low shear to practically zero (with the stator in the second position) are taken care of.
- a homogenizer 1 which has a substantially circular cylindrical housing 2, in which one below with reference to Fig. 2 to 4 rotor / stator system explained in more detail as well as a mixing and a conveying device with a conveying element designed in the manner of a screw conveyor are rotatably mounted on a shaft extending axially in the housing 2.
- a controllable drive motor (not shown) is mounted to the shaft of the rotor and the conveying and mixing device with the respective desired speed in rotation to be able to put.
- the housing 2 of the homogenizer 1 is provided with an inlet 4 for applying the flowable substances to be homogenized or dispersed.
- further inlets 4a may be provided to enforce additional substances to be mixed into the flowable substances and / or to connect measuring devices such as thermometers, barometers or the like or to make the housing 2 more accessible, for example for the purpose a cleaning, wherein the inlets 4a, for example by means of cover (not shown) are closed.
- a radially arranged outlet 5 for the mixed / homogenized product which also here additional outlets 5a (see, in this regard, the sectional view of Fig. 2 , in the sectional plane of the main outlet 5 is not recognizable for the product) may be provided, which serve largely for the same purposes as the above-mentioned, optional additional inlets 4a and also by means of lid (not shown) can be closed.
- the homogenizer 1 may for example be part of an in Fig. 1 Not shown homogenizing be, which comprises a stirred tank (also not shown), from which branches off a line opening into the inlet 4 of the homogenizer 1 line.
- the outlet 5 of the homogenizer either flows back into the stirred tank or feeds the finished homogenized product to further processing steps or to a filling.
- Fig. 2 and 3 it can be seen extending inside the housing 2 of the homogenizer 1 with the seated on the flange 3 drive (not shown), for example via a shaft coupling 11, connected shaft 12, which by means of a seal 13, such as a mechanical seal against the flange is sealed.
- a seal 13 such as a mechanical seal against the flange is sealed.
- the conveyor 25 and the rotor 16 are thus in the present case together by means of the drive (not shown) in rotation displaceable, wherein the rotor 16 optionally decoupled from the drive can be, for example, by axial displacement of the shaft 12 in the direction of the flange 3 (arrow P of Fig. 3 ), so that the free end 12 a of the shaft 12 is disengaged from the rotor 16.
- the rotor 16 comprises in the present embodiment, an outer rotor blade 16a and an inner rotor blade 16b, which are arranged coaxially with each other and driven in rotation by the shaft 12 together.
- Both rotor blades 16a, 16b are provided in axial directions with openings, which in particular are aligned with each other and ensure a more or less unobstructed axial passage of the product.
- the rotor blades 16a, 16b have substantially the shape of a cylinder jacket with openings, or slots, in particular of different size and shape, which are released in the circumferential direction.
- the openings or slots 22 of the outer rotor blade 16a are formed, for example, approximately rectangularly between the cylinder jacket defining, blade-like elements, while the openings 21 of the inner rotor blade 16b are formed for example by the cylinder jacket passing through slots.
- the stator 17 arranged radially in a first position between the outer 16a and the inner rotor blade 16b also has substantially the shape of a cylinder jacket and is also open in the axial direction.
- distributed openings 23 of the stator 17 have, for example, a slot shape of smaller width than the openings / slots 21,22 of the rotor blades 16a, 16b.
- stator 17 engages the stator 17 in a first position in each case to form a radial shear gap between the rotor blades 16a, 16b of the rotor 16 to provide for homogenization or dispersion of the product due to the introduction of shear forces, wherein the stator 17 in at least a first position, for example substantially over its entire axial extent radially between the rotor blades 16a, 16b of the rotor 16 is arranged.
- the conveying device 25 has, as already indicated above, approximately helical conveying elements 26, which extend around at least a portion of the circumference of its axis of rotation, ie the shaft 12, and from there to the area of the surrounding inner wall of the housing 2, leaving only one narrow gap of, for example, about 0.5 mm.
- the inner wall of the housing 2 narrows (viewed in the conveying direction) in the region of the conveying elements 26 for the purpose of a suitable pressure build-up in the homogenizer 1, wherein the free - toysss worne- end of the conveying elements 26, for example, according to the taper of the inner wall of the housing 2 provided with a chamfer can be (cf. Fig. 2 ).
- the homogenizer 1 is equipped with a mixing device 15, which in the present embodiment, upstream of the conveyor 25, for example, between this and the rotor 16, is arranged, but also downstream thereof may be positioned (not shown).
- the mixing device 15 has in the drawing reproduced embodiment, a plurality of fixed to the shaft 12 mixing vanes 14, which are arranged slightly inclined with respect to their axis of rotation and thus configured substantially in the form of propellers and each only a part of the scope of their Extend axis in the form of the shaft 12, wherein they are arranged distributed in the circumferential direction thereof.
- the mixing blades extend 14, for example, at an angle of about 30 ° to 60 ° around the circumference of the axis of rotation, wherein - also viewed in the circumferential direction - between the mixing vanes 14, an at least about the same size or larger contrast gap is provided.
- the mixing blades 14 may be provided with perforations, which additionally provide for a gentle mixing or homogenizing effect.
- the stator 17 is, as already indicated, in the in Fig. 2 illustrated operating situation in a first position in which it is in each case radially adjacent to the rotor 16 - or more precisely: radially between the two rotor elements 16a, 16b - is arranged so that between the stator 17 and the two rotor elements in each case a shearing gap is formed downstream of the same the homogenized product leaves the housing 2 of the homogenizer 1 via the outlet 5.
- the stator 17, as in particular from Fig. 2 and 3 at least between this first position and a second, in Fig.
- an actuator 30 is provided for this purpose, which comprises, for example, several (here: three) fluidly, eg hydraulically actuated, piston / cylinder units 31 whose pistons are mounted on a carrier 32 (FIG. Fig. 2 ) of the actuator 30 are mounted and their cylinder with the in Fig.
- stator 17 is moved into its first, in Fig. 2 shown position in the direction of arrow V (in Fig. 2 to the left); If, on the other hand, the pistons of the piston / cylinder units 31 are evacuated, then the stator 17 is displaced to the right in the direction of the arrow V, until it abuts, for example, against a stop predetermined by the stop of the pistons in the cylinders, in which case it is preferably below a certain limit axial distance from the rotor 16 of, for example, a few millimeters is arranged. Because of the drive of the shaft 3 independent actuator 30, such a displacement of the stator 17 during the operation of the homogenizer 1, that is done with a rotating rotor 16.
- the actuator 30 of the stator 17 is fixed in the embodiment shown on a front side of the housing 2 of the homogenizer 1 closing lid 33, which of a with a fluid connection 35 (FIG. Fig. 1 ) cap 34 (in Fig. 3 not shown) can be closed to accommodate the actuator 30 protected from external influences.
- the cover 33 with the actuator 30 of the housing 2 is removable and against a in the Fig. 4 reproduced cover 40 with a frontal inlet opening 41 for the task of such a substance component interchangeable.
- the cover 33 with the actuator 30 of the housing 2 is removable and against a in the Fig. 4 reproduced cover 40 with a frontal inlet opening 41 for the task of such a substance component interchangeable.
- the homogenizer 1 according to Fig. 1 to 3 can operate essentially in two different operating modes, on the one hand in a "shear mode" according to conventional homogenizers with a rotor / stator system, on the other hand in a pure “pump mode” bypassing the or between the rotor 16 and stator 17 formed shear gap (s):
- stator 17 In “shear mode", the stator 17 is in the in Fig. 2 reproduced first position, in each of which a radial shear gap between the stator 17 and the rotor blades 16a, 16b is formed.
- the product to be homogenized enters via the inlet 4 in the housing 2 of the homogenizer 1, passes the mixing device 15 over the conveyor 25 to the rotor / stator 16, 17, wherein it under high shear between the rotor blades 16 a, 16 b and the shear column formed by the stator 17 passes through and leaves the homogenizer 1 through the outlet 5.
- the rotational speed of the rotor / stator system 16, 17 are freely selected by means of the controllable drive.
- the conveyor 25 rotates in the "shear mode" together with the rotor 16 and the mixing device 15, which ensures a certain pre-homogenization.
- the stator 17 In "pump mode", the stator 17 is located in the Fig. 2 reproduced first position shifted so far to the right in the second position that it is arranged axially adjacent to the rotor 16 and consequently no radial shear gap between the stator 17 and the rotor blades 16a, 16b longer exists.
- the product to be homogenized in turn enters the housing 2 of the homogenizer 1 via the inlet 4, passes the mixing device 15 and via the conveyor 25 to the rotor blades 16a, 16b of the rotor 16, which radially displaces it while avoiding the passage of a shear gap penetrated outside, after which it leaves the homogenizer 1 through the outlet 5.
- the conveyor 25 is able to ensure a sufficient flow rate even at low speeds, while the mixing device 15, a very gentle homogenizing effect when passing the, provided here with the perforations, mixing blades 14 is ensured.
- the rotor 16, the conveyor 25 and the mixing device 15 common drive 4 is provided, as is the case in the present embodiment, the rotor 16 rotates in the "pumping mode" together with the conveyor 25 and the mixing device 15 with but, if desired, can also be decoupled from the shaft 12.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Liquid Crystal Substances (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
- Disintegrating Or Milling (AREA)
- Saccharide Compounds (AREA)
Abstract
Description
Die Erfindung betrifft einen Homogenisator zur Homogenisierung oder Dispergierung von fließfähigen Stoffen, mit einer wenigstens einen Rotor tragenden, drehbar gelagerten und mittels eines, insbesondere steuerbaren, Antriebs in Rotation versetzbaren Welle und mit einem mit dem Rotor zusammenwirkenden Stator, wobei zwischen dem Rotor und dem Stator wenigstens ein Scherspalt gebildet ist. Die Erfindung bezieht sich ferner auf eine Homogenisiervorrichtung zur Homogenisierung oder Dispergierung von fließfähigen Stoffen, mit einem insbesondere mit einem Rückwerk ausgestatteten Behälter mit wenigstens einer von dem Behälter abzweigenden und in einen Einlaß eines Homogenisators der vorgenannten Art führenden Abzweigleitung.The invention relates to a homogenizer for the homogenization or dispersion of flowable materials, with a rotatably mounted at least one rotor, and rotatable by means of a, in particular controllable, drive rotatable shaft and with a rotor cooperating with the stator, wherein between the rotor and the stator at least one shear gap is formed. The invention further relates to a homogenizer for homogenizing or dispersing flowable materials, with a particular equipped with a return container with at least one branching off of the container and leading into an inlet of a homogenizer of the aforementioned type branch line.
Solche Homogenisatoren finden zur Homogenisierung oder Dispergierung von fließfähigen Stoffen, wie flüssigen bis hin zu mehr oder minder viskosen Stoffen oder Stoffgemischen, z.B. Emulsionen, Dispersionen etc., verbreiteten Einsatz, beispielsweise in der chemischen, pharmazeutischen, kosmetischen und Lebensmittelindustrie. Dabei werden die Homogenisatoren häufig gemeinsam mit einem Rührbehälter betrieben, wobei der Homogenisator in einer von dem Behälter abgehenden und gegebenenfalls in diesen zurückführenden Leitung, vorzugsweise auf einem Niveau im Bereich der tiefsten Stelle des Behälters oder unterhalb desselben, angeordnet sein kann, so daß der Homogenisator zusätzlich zu dem Rührwerk des Behälters zu einer einwandfreien Homogenisierung oder Dispergierung des Produktes beiträgt. Die Homogenisierwirkung beruht vornehmlich auf dem Eintrag von Scherkräften auf die fließfähigen Stoffe durch Drehung des Rotors, welcher mit dem demgegenüber ruhenden Stator zusammenwirkt. Der Rotor kann ein oder mehrere Rotorblätter aufweisen, z.B. jeweils ein zu beiden Seiten des Stators angeordnetes Rotorblatt, welche jeweils einen Scherspalt zwischen sich und dem Stator begrenzen. Im Vergleich mit andersartigen Homogenisatoren, wie Hochdruck- oder Ultraschallhomogenisatoren, bieten gattungsgemäße Homogenisatoren den Vorteil eines demgegenüber einfacheren und kostengünstigeren Aufbaus sowie insbesondere eines verschleißärmeren Betriebs.Such homogenizers are widely used for the homogenization or dispersion of flowable substances, such as liquid to more or less viscous substances or mixtures of substances, for example emulsions, dispersions, etc., for example in the chemical, pharmaceutical, cosmetic and food industries. It will be the homogenizers often operated together with a stirred tank, wherein the homogenizer in a outgoing from the container and optionally in this recirculating line, preferably at a level in the region of the lowest point of the container or below it, may be arranged, so that the homogenizer in addition to the agitator of the container contributes to a proper homogenization or dispersion of the product. The homogenizing effect is based primarily on the entry of shear forces on the flowable substances by rotation of the rotor, which cooperates with the counterpart stationary stator. The rotor may have one or more rotor blades, for example, in each case one arranged on both sides of the stator rotor blade, each defining a shearing gap between itself and the stator. In comparison with other types of homogenizers, such as high-pressure or ultrasonic homogenizers, generic homogenizers offer the advantage of a simpler and more cost-effective design and, in particular, a lower-wear operation.
Um die Homogenisierwirkung - oder genauer: die in die fließfähigen Stoffe eingetragenen Scherkräfte - einstellen zu können, kann die Drehzahl des Rotors in Bezug auf den stationären Stator steuerbar sein, wobei die Scherwirkung mit steigender Drehzahl des Rotors zunimmt. Zugleich nimmt die Förderwirkung des Homogenisators bei steigender Drehzahl seines Rotors zu, so daß die Förderwirkung unmittelbar an die Scherwirkung des Homogenisators gekoppelt ist. Dies ist in der Regel dadurch bedingt, daß aufgrund der Relativbewegung zwischen Rotor und Stator in dem zwischen dem Rotor und dem Stator gebildeten Scherspalt ein drehzahlabhängiger Unterdruck erzeugt wird, welcher das zu verarbeitende Produkt ansaugt und durch den Spalt hindurch nach radial außen drückt. Eine Verarbeitung von gegenüber Scherkräften empfindlichen Stoffen ist somit nur bedingt möglich, da ein zur Förderung des Produktes durch den zwischen dem Rotor und dem Stator gebildeten Scherspalt hinreichender Unterdruck erst ab einer gewissen Drehzahl erreicht werden kann, die wiederum ein gewisses Mindestmaß an auf das Produkt wirkende Scherkräfte bedingt. Entsprechendes gilt für die Dispergierung von gegenüber mechanischer Einwirkung empfindlichen Feststoffpartikeln, welche z.B. in ein flüssiges oder viskoses Medium eindispergiert werden sollen und auf diese Weise Gefahr laufen, in dem Scherspalt zerkleinert zu werden.In order to be able to set the homogenizing effect or, more precisely, the shear forces introduced into the flowable substances, the rotational speed of the rotor with respect to the stationary stator can be controllable, the shear effect increasing with increasing rotational speed of the rotor. At the same time the conveying effect of the homogenizer increases with increasing speed of its rotor, so that the conveying effect is coupled directly to the shearing action of the homogenizer. This is usually due to the fact that due to the relative movement between the rotor and stator in the shear gap formed between the rotor and the stator, a speed-dependent negative pressure is generated, which is to be processed Suction product and push through the gap radially outward. Processing of substances sensitive to shear forces is thus only possible to a certain extent, since a negative pressure sufficient for conveying the product through the shear gap formed between the rotor and the stator can only be achieved at a certain speed, which in turn has a certain minimum effect on the product Shearing forces conditionally. The same applies to the dispersion of sensitive to mechanical action solid particles, which are to be dispersed eg in a liquid or viscous medium and thus run the risk of being crushed in the shear gap.
Die
Darüber hinaus ist es bekannt, anstelle eines oder zusätzlich zu einem Stator einen weiteren, separat angetriebenen Rotor vorzusehen, so daß die Scherwirkung des Homogenisators durch individuelles Einstellen der Drehzahl beider Rotoren mit gegen- oder gleichsinniger Drehung eingestellt werden kann. Indes erfordern solche Homogenisatoren einen relativ hohen konstruktiven Aufwand mit zwei separaten Antrieben einschließlich der zugehörigen Lagerungen und Dichtungen, welcher mit einem verhältnismäßig hohen Kostenaufwand einhergeht. Insbesondere ist auch in diesem Fall eine Verarbeitung von sehr scherempfindlichen Stoffen und/oder von gegenüber mechanischer Einwirkung empfindlichen Feststoffpartikeln nicht möglich, zumal - wie bereits erwähnt - die Förderwirkung auch hier unmittelbar von der Scherwirkung abhängt. Die
Der Erfindung liegt die Aufgabe zugrunde, einen Homogenisator der eingangs genannten Art auf einfache und kostengünstige Weise dahingehend weiterzubilden, daß seine Scherwirkung bei fortwährender Förderwirkung auf ein minimales Maß begrenzt werden kann, um ihm auch einen Einsatz für die Verarbeitung sowohl sehr scherempfindlicher Stoffe als auch gegenüber mechanischer Einwirkung empfindlicher Feststoffpartikel zu erschließen.The invention has the object of providing a homogenizer of the type mentioned in a simple and cost-effective way to the effect that its shearing effect can be limited to a minimum extent with continuous promotion, to him also an application for the processing of both very shear-sensitive substances as well to develop mechanical action of sensitive solid particles.
Erfindungsgemäß wird diese Aufgabe bei einem Homogenisator der eingangs genannten Art sowie bei einer mit einem solchen Homogenisator ausgestatteten Homogenisiervorrichtung der eingangs genannten Art dadurch gelöst, daß der Stator in Bezug auf den Rotor zwischen wenigstens einer ersten Position, in welcher zumindest ein axialer Abschnitt des Stators unter Bildung des Scherspaltes radial neben dem Rotor angeordnet ist, und einer zweiten Position, in welcher der Stator in Axialrichtung neben dem Rotor angeordnet ist, so daß zwischen Rotor und Stator kein Scherspalt mehr vorhanden ist, axial verlagerbar ist.According to the invention this object is achieved in a homogenizer of the type mentioned and in a homogenizer equipped with such a homogenizer of the type mentioned in that the stator with respect to the rotor between at least a first position, in which at least an axial portion of the stator below Forming the shear gap is arranged radially adjacent to the rotor, and a second position in which the stator is arranged in the axial direction adjacent to the rotor, so that between the rotor and stator no shear gap is present, is axially displaceable.
Die erfindungsgemäße Ausgestaltung macht es auf konstruktiv einfache Weise möglich, daß die Scherwirkung bei fortwährender, zumindest durch die Rotation des Rotors bewirkter Förderleistung durch den Homogenisator hindurch auf ein gegenüber dem Stand der Technik ungleich geringeres Niveau bis hin zu praktisch null abgesenkt werden kann, indem das fließfähige Produkt an dem von dem Rotor fort verlagerten Stator vorbeigeführt wird, das Rotor-/Statorsystem folglich "gebypaßt" wird. Hierzu wird der Stator in seine zweite Position verlagert, in welcher er axial neben dem Rotor angeordnet ist und der zwischen ihm und dem Rotor in Radialrichtung gebildete Scherspalt folglich nicht mehr vorhanden ist. Die fließfähigen Stoffe werden nun lediglich durch die von dem Rotor bewirkten Zentrifugalkräfte, gegebenenfalls unterstützt von einer Fördereinrichtung (siehe hierzu weiter unten), durch den Homogenisator hindurch gefördert, wodurch gar keine oder allenfalls sehr geringe Scherkräfte in das Produkt oder in die - beispielsweise aus einer flüssigen oder viskosen Matrix mit hierin eindispergierten, gegen mechanische Beanspruchung empfindlichen Feststoffpartikel gebildete - Produktmischung eingetragen werden, aber gleichwohl für eine gewisse, sehr schonenden Misch-/Homogenisierwirkung gesorgt wird. Sollen demgegenüber stärkere Scherkräfte in das Produkt eingetragen werden, so wird der Stator in seine wenigstens eine erste Position verlagert, in welcher er zumindest teilweise radial neben dem Rotor angeordnet ist und zwischen sich und dem Rotor einen Scherspalt bildet. Der erfindungsgemäße Homogenisator läßt sich folglich einerseits in einem für gattungsgemäße Homogenisatoren üblichen "Schermodus", in welchem sich der Stator in der ersten Position befindet, andererseits in einem bei bekannten gattungsgemäßen Homogenisatoren bislang nicht möglichen, reinen "Pumpmodus" betreiben, in welchem sich der Stator in der zweiten Position befindet und das fließfähige Produkt lediglich durch den Stator hindurch gefördert wird. Darüber hinaus kann selbstverständlich - sofern gewünscht - die Drehzahl des Rotors, vorzugsweise unabhängig von der jeweiligen Position des Stators, variabel sein, um die Scher- und/oder Förderwirkung des Homogenisators verändern zu können.The inventive design makes it possible in a structurally simple manner that the shearing effect can be lowered by a constant, at least by the rotation of the rotor effected flow through the homogenizer on a comparison with the prior art unequal lesser level up to virtually zero by the flowable product is passed past the rotor displaced from the stator, the rotor / stator system is thus "bypassed". For this purpose, the stator is displaced into its second position in which it is arranged axially next to the rotor and consequently the shearing gap formed between it and the rotor in the radial direction is no longer present. The flowable substances are now only by the centrifugal forces caused by the rotor, possibly supported by a conveyor (see below), conveyed through the homogenizer through which no or at most very low shear forces in the product or in the - for example from a liquid or viscous matrix with herein einispergierten, against mechanical stress sensitive solid particles formed product mixture are registered, but nevertheless provided for a certain, very gentle mixing / homogenizing effect. If, on the other hand, stronger shear forces are to be introduced into the product, then the stator is displaced into its at least one first position, in which it is arranged at least partially radially next to the rotor and forms a shear gap between itself and the rotor. The homogenizer according to the invention can therefore be, on the one hand, in a "shear mode", which is usual for generic homogenizers, in which the stator is in the first position, on the other hand operate in a conventional generic homogenizers so far not possible, pure "pump mode" in which the stator is in the second position and the flowable product is conveyed through the stator only. In addition, of course - if desired - the speed of the rotor, preferably independently of the respective position of the stator, be variable in order to change the shearing and / or conveying action of the homogenizer can.
Um eine Produktscherung bei dem in der zweiten Position befindlichen Stator zuverlässig zu verhindern, kann es von Vorteil sein, wenn der Stator in der zweiten Position mit einem gewissen axialen Abstand, beispielsweise von wenigstens 1 mm, vorzugsweise von wenigstens 2 mm, insbesondere von wenigstens 5 mm, von dem Rotor angeordnet ist. Darüber hinaus kann es zweckmäßig sein, wenn der Stator in der zweiten Position gegen einen auf der dem Rotor abgewandten Seite des Stators angeordneten Anschlag anstößt, um auf konstruktiv sehr einfache Weise für eine fest vorgegebene zweite Position des Stators zu sorgen, in welcher er eine Produktscherung zuverlässig verhindert.In order to reliably prevent product shearing in the stator located in the second position, it may be advantageous if the stator in the second position with a certain axial distance, for example of at least 1 mm, preferably of at least 2 mm, in particular of at least 5 mm, is arranged by the rotor. In addition, it may be expedient if the stator abuts in the second position against a stop arranged on the side facing away from the rotor of the stator, in order to provide a structurally very simple way for a fixed predetermined second position of the stator, in which he product shear reliably prevented.
In vorteilhafter Ausgestaltung kann vorgesehen sein, daß der Stator in wenigstens einer ersten Position im wesentlichen über seine gesamte axiale Erstreckung radial neben dem Rotor angeordnet ist, um für eine - wie gesagt, gegebenenfalls zusätzlich durch die Rotationsgeschwindigkeit des Rotors variierbaren - Scherung des Produktes und somit für einen möglichst hohen Wirkungsgrad des Homogenisators im "Schermodus" zu sorgen.In an advantageous embodiment, it may be provided that the stator is arranged in at least a first position substantially over its entire axial extent radially adjacent to the rotor, for a - as I said, optionally additionally variable by the rotational speed of the rotor - shear of the product and thus to ensure the highest possible efficiency of the homogenizer in the "shear mode".
Während es grundsätzlich zum Erreichen der erfindungsgemäßen Funktion des Homogenisators ausreicht, wenn der Stator ausschließlich zwischen einer (einzigen) ersten Position und der zweiten Position in Bezug auf den Rotor verlagerbar ist, kann selbstverständlich auch vorgesehen sein, daß der Stator ferner zwischen mehreren ersten Positionen, in welchen der Stator jeweils zumindest mit einem axialen Abschnitt radial neben dem Rotor angeordnet ist, in Bezug auf den Rotor verlagerbar ist. Im letztgenannten Fall kann die - in den verschiedenen ersten Positionen des Stators stets vorhandene - Scherwirkung durch Vergrößerung bzw. Verkleinerung des zwischen Rotor und Stator gebildeten Scherspaltes weiter variiert werden.While it is basically sufficient for achieving the function of the homogenizer according to the invention, when the stator is displaceable exclusively between a (single) first position and the second position with respect to the rotor, it can of course also be provided that the stator is connected between a plurality of first positions, in which the stator is arranged in each case at least with an axial portion radially adjacent to the rotor, with respect to the rotor is displaceable. In the latter case, the shearing action, which is always present in the various first positions of the stator, can be further varied by increasing or decreasing the shearing gap formed between the rotor and the stator.
Wie bereits angedeutet, ist es in konstruktiver Hinsicht günstig, wenn der Rotor axialfest angeordnet und der Stator in Axialrichtung verlagerbar ist, wobei grundsätzlich auch der Rotor axialfest und der Stator demgegenüber axial verschieblich angeordnet sein kann.As already indicated, it is favorable in terms of design, if the rotor axially fixed and the stator is displaced in the axial direction, in principle, the rotor axially fixed and the stator can be arranged axially displaceable contrast.
In vorteilhafter Weiterbildung des erfindungsgemäßen Homogenisators kann vorgesehen sein, daß dem aus Rotor und Stator gebildeten Rotor-/Statorsystem eine Fördereinrichtung vorgeordnet ist. Mittels einer solchen Fördereinrichtung kann insbesondere im "Pumpmodus" (d.h. mit dem in der zweiten Position befindlichen Stator) auch bei sehr geringer Drehzahl des Rotors und folglich sehr geringen, hierdurch bewirkten Zentrifugalkräften auf die fließfähigen Stoffe bei einer sehr schonenden Mischung/Homogenisierung eine hinreichende Förderleistung des Produktes durch den Homogenisator hindurch sichergestellt werden. Sofern insbesondere, wie oben erwähnt, ein axialfester Stator und ein demgegenüber in die zweite Position verlagerbarer Rotor vorgesehen ist, kann eine solche Fördereinrichtung auch gänzlich für die im "Pumpmodus" erforderliche Förderleistung dienen.In an advantageous development of the homogenizer according to the invention, provision can be made for a conveying device to be arranged upstream of the rotor / stator system formed by the rotor and the stator. By means of such a conveyor, in particular in the "pumping mode" (ie with the stator located in the second position) even at very low speed of the rotor and consequently very small, thereby caused centrifugal forces on the flowable materials at a very gentle mixture / homogenization, a sufficient flow rate of the product through the homogenizer. If, in particular, as mentioned above, an axially fixed stator and a counterpart in the second position displaceable rotor provided is, such a conveyor can also serve entirely for the required in the "pumping mode" capacity.
Eine besonders bevorzugte Ausführungsform sieht vor, daß es sich bei dem erfindungsgemäßen Homogenisator um einen sogenannten "externen Homogenisator" handelt, bei welchem das Rotor-/Statorsystem und gegebenenfalls die Fördereinrichtung in einem eigenen Gehäuse aufgenommen sind, in welchem die den Rotor tragende Welle gelagert ist.A particularly preferred embodiment provides that the homogenizer according to the invention is a so-called "external homogenizer" in which the rotor / stator system and optionally the conveyor are accommodated in a separate housing in which the shaft carrying the rotor is mounted ,
Das Gehäuse weist hierbei vorzugsweise wenigstens einen stromauf des Rotor-/Statorsystems angeordneten Einlaß auf, welcher insbesondere an eine Abzweigleitung eines, insbesondere mit einem Rührwerk ausgestatteten, Behälters anschließbar ist. Darüber hinaus weist das Gehäuse bevorzugt wenigstens einen stromab des Rotor-/Statorsystems angeordneten Auslaß auf, welcher insbesondere an eine Rückführleitung des, insbesondere mit einem Rührwerk ausgestatteten, Behälters anschließbar ist. Der Homogenisator ist auf diese Weise Teil einer Kreislaufleitung aus dem (Rühr)behälter einer Homogenisiervorrichtung und in diesen hinein, um für eine sehr effektive Mischung/Homogenisierung der Produkte wahlweise im "Schermodus" und/oder im "Pumpmodus" zu sorgen. Alternativ ist es selbstverständlich auch denkbar, daß - sofern der Homogenisator als Teil einer Homogenisiervorrichtung an deren (Rühr)behälter angeschlossen ist - das homogenisierte Produkt über seinen Auslaß z.B. auch weiteren Verarbeitungsschritten bzw. einer Abfüllung zugeführt wird, anstelle es in den (Rühr)behälter zu rezirkulieren.In this case, the housing preferably has at least one inlet arranged upstream of the rotor / stator system, which inlet can be connected in particular to a branch line of a container, in particular equipped with an agitator. In addition, the housing preferably has at least one outlet arranged downstream of the rotor / stator system, which outlet can be connected in particular to a return line of the container, in particular equipped with an agitator. The homogenizer is in this way part of a circulation line from the (stirring) container of a homogenizer and into it, in order to ensure a very effective mixing / homogenization of the products either in the "shear mode" and / or in the "pumping mode". Alternatively, it is of course also conceivable that - if the homogenizer is connected as part of a homogenizer to the (stirring) container - the homogenized product through its outlet, for. is also supplied to further processing steps or a bottling, instead of recirculating it in the (stirring) container.
Die Begriffe "stromauf" bzw. "stromab" beziehen sich in diesem Zusammenhang stets auf die vorgesehene Förderrichtung der fließfähigen Stoffe durch den Homogenisator hindurch, d.h. von seinem Einlaß, gegebenenfalls über die Fördereinrichtung und das Rotor-/Statorsystem hin zu seinem Auslaß. Die vorzugsweise vorhandene Fördereinrichtung kann hierbei im übrigen stromauf oder stromab des Rotors angeordnet sein, wobei es grundsätzlich auch möglich ist, sowohl eine stromauf als auch eine stromab des Rotors angeordnete Fördereinrichtung vorzusehen.The terms "upstream" and "downstream" in this context always refer to the intended conveying direction of the flowable substances through the homogenizer, ie from its inlet, optionally via the conveyor and the rotor / stator system to its outlet. The preferably present conveying device can be arranged otherwise upstream or downstream of the rotor, wherein it is also possible in principle to provide both an upstream and downstream of the rotor arranged conveyor.
Der Auslaß des Homogenisators ist in diesem Fall zweckmäßig radial in Bezug auf die den Rotor tragenden Welle und im axialen Bereich des Rotor-/Statorsystems angeordnet, so daß das gemischte/homogenisierte Produkt nach Passieren des Rotor-/Statorsystems bzw. - bei in der zweiten Position befindlichem Stator - des Rotors das Gehäuse des Homogenisators radial verläßt. Um für eine möglichst hohe Förderwirkung zu sorgen, kann es hierbei von Vorteil sein, wenn sich das Rotor-/Statorsystem radial bis in den Bereich der Innenwand des Gehäuses erstreckt.The outlet of the homogenizer is expediently arranged radially with respect to the shaft carrying the rotor and in the axial region of the rotor / stator system, so that the mixed / homogenized product after passing through the rotor / stator system or - in the second Positioning stator - the rotor leaves the housing of the homogenizer radially. In order to ensure the highest possible conveying effect, it may be advantageous in this case if the rotor / stator system extends radially into the region of the inner wall of the housing.
Sofern der Homogenisator mit einer Fördereinrichtung ausgestattet ist, kann diese z.B. wenigstens ein koaxial mit der Welle des Rotors in Rotation versetzbares Förderelement aufweisen, welches beispielsweise in Form eines Schneckenelementes einer Förderschnecke ausgebildet sein kann und sich zweckmäßig um zumindest einen Teil des Umfangs seiner Drehachse erstreckt. Um für eine zufriedenstellende Förderwirkung auch bei schonendem Betrieb des Homogenisators im "Pumpmodus" bei geringer Drehzahl der Fördereinrichtung zu sorgen, wenn sich der Stator in der zweiten Position befindet, erstreckt sich das Förderelement vorzugsweise bis in den Bereich der Innenwand des Gehäuses, so daß der fließfähige Stoff zumindest nicht in nennenswertem Umfang zwischen dem Förderelement und der Innenwand des Gehäuses hindurch an dem Förderelement vorbei fließen kann. Selbstverständlich kann zwischen dem freien Ende des Förderelementes und der Innenwand des Gehäuses ein geringer Spalt, z.B. mit einer Breite von höchstens etwa 2 mm oder von höchstens etwa 1 mm gebildet sein, um einen verschleißarmen Betrieb der Fördereinrichtung zu gewährleisten. Darüber hinaus kann es zum Zwecke eines Druckaufbaus von Vorteil sein, wenn die Fördereinrichtung (z.B. deren wenigstens eines Förderelement) an einem sich innenseitig verengenden Abschnitt des Gehäuses angeordnet ist, wobei sich der Begriff "verengend" auf die Förderrichtung der fließfähigen Stoffe durch den Homogenisator hindurch bezieht.If the homogenizer is equipped with a conveying device, it may, for example, have at least one conveying element that can be rotated coaxially with the shaft of the rotor, which may be designed, for example, in the form of a screw element of a screw conveyor and expediently extends around at least a part of the circumference of its axis of rotation. In order to ensure a satisfactory conveying effect even with gentle operation of the homogenizer in the "pumping mode" at low speed of the conveyor when the stator is in the second position, the conveying element preferably extends into the region of the inner wall of the housing, so that the flowable material at least not to a significant extent between the conveyor element and the inner wall of the housing can flow past the conveyor element. Of course, between the free end of the conveying element and the inner wall of the housing, a small gap, for example, be formed with a width of at most about 2 mm or at most about 1 mm, to ensure a low-wear operation of the conveyor. In addition, it may be for the purpose of pressure build-up advantageous if the conveyor (eg at least one conveying element) is disposed on a narrowing of the inner side portion of the housing, wherein the term "narrowing" on the conveying direction of the flowable substances through the homogenizer refers.
Gemäß einer Weiterbildung des erfindungsgemäßen Homogenisators kann ferner eine Mischeinrichtung vorgesehen sein, deren Anordnung in Bezug auf das Rotor-/Statorsystem und/oder auf die Fördereinrichtung stromauf oder stromab derselben oder auch zwischen diesen gewählt sein kann. In diesem Fall ist es insbesondere möglich, beim schonenden Betrieb des Homogenisator im "Pumpmodus" mit in der zweiten Position befindlichem Stator für eine erhöhte, aber gleichwohl sehr scherarme Homogenisierung/Dispergierung der fließfähigen Stoffe aufgrund der Homogenisierwirkung der zusätzlichen Mischeinrichtung zu sorgen. Darüber hinaus kann die Mischeinrichtung selbstverständlich auch beim herkömmlichen Betrieb des Homogenisators im "Schermodus" eine zusätzliche Homogenisierung/Dispergierung oder - sofern die Mischeinrichtung stromauf des Rotors angeordnet ist - eine gewisse Vorhomogenisierung bewirken. In jedem Fall eröffnet eine solche Ausgestaltung dem Homogenisator einen praktisch für beliebige fließfähige Stoffe geeigneten Einsatz, seien sie relativ unempfindlich oder auch hoch empfindlich gegen Scherkräfte bzw. gegen mechanische Beanspruchung.According to a development of the homogenizer according to the invention, a mixing device may further be provided, the arrangement of which may be selected upstream or downstream thereof or also between the rotor / stator system and / or on the conveyor. In this case, it is possible, in particular, to ensure, during the gentle operation of the homogenizer in the "pumping mode" with the stator in the second position, an increased but nevertheless very low shear homogenization / dispersion of the flowable substances due to the homogenizing effect of the additional mixing device. In addition, the mixer can of course also in the conventional operation of the homogenizer in the "shear mode" additional homogenization / dispersion or - if the mixing device is arranged upstream of the rotor - cause some pre-homogenization. In any case, such a configuration opens the homogenizer a practically suitable for any flowable materials use, they are relatively insensitive or highly sensitive to shear forces or against mechanical stress.
Die Mischeinrichtung kann vorzugsweise wenigstens einen oder insbesondere auch mehrere, koaxial mit der Drehachse des Rotors in Rotation versetzbare(n) Mischflügel aufweisen, welche(r) sich in vorteilhafter Ausführung (jeweils) nur um einen Teil des Umfangs ihrer Drehachse erstreckt/erstrecken. Darüber hinaus können mehrere Mischflügel bevorzugt mit radialem und/oder axialem Abstand voneinander angeordnet sein, so daß eine gleichförmige, schonende Durchmischung bzw. Homogenisierung des Produktes über den gesamten Querschnitt des Homogenisators möglich ist. Darüber hinaus kann/können der/die Mischflügel der Mischeinrichtung in Bezug auf ihre Drehachse schräg angeordnet sein, wodurch die Misch- bzw. Homogenisierwirkung verbessert und gegebenenfalls eine zusätzliche Förderwirkung induziert werden kann; die Mischflügel können dabei beispielsweise eine etwa propellerartige Gestalt besitzen. Ferner kann/können der/ die Mischflügel perforiert sein, um für eine weiterhin verbesserte Misch- bzw. Homogenisierwirkung zu sorgen und dabei einen (geringen) Stoffstrom durch die Mischflügel hindurch zu ermöglichen. Indes kann die Mischeinrichtung alternativ oder zusätzlich zu solchen Mischflügeln selbstverständlich auch beliebige andersartig ausgestaltete Mischelemente besitzen. Lediglich beispielhaft seien in diesem Zusammenhang sich z.B. zumindest teilweise in Radialrichtung erstreckende Mischstäbe erwähnt, welche beispielsweise an der Drehachse der Mischeinrichtung festgelegt sein und gegebenenfalls mit stationär an der Innenwand des Gehäuses des Homogenisators unter axialem Versatz hierzu angeordneten stationären, z.B. ebenfalls stabförmigen, Elementen zusammenwirken können.The mixing device may preferably have at least one or in particular a plurality of mixing vanes which can be set into rotation coaxially with the axis of rotation of the rotor and which advantageously extend (only) around part of the circumference of its axis of rotation. In addition, a plurality of mixing vanes may preferably be arranged with radial and / or axial distance from each other, so that a uniform, gentle mixing or homogenization of the product over the entire cross-section of the homogenizer is possible. In addition, the mixing blade (s) of the mixing device can be arranged obliquely with respect to its axis of rotation, as a result of which the mixing or homogenizing effect can be improved and optionally an additional conveying effect can be induced; The mixing blades can have, for example, an approximately propeller-like shape. Further, the mixing blade (s) may be perforated to provide a further improved mixing or homogenizing effect thereby allowing a (small) flow of material through the mixing blades. However, the mixing device can of course also have any differently configured mixing elements as an alternative or in addition to such mixing blades. By way of example only, in this context, for example at least partially in the radial direction extending mixing rods are mentioned, which may for example be fixed to the axis of rotation of the mixing device and optionally with stationary stationary on the inner wall of the housing of the homogenizer with axial offset thereto arranged stationary, for example, also rod-shaped elements can cooperate ,
Um für eine konstruktiv sehr einfache und kostengünstige Ausgestaltung zu sorgen, können der Rotor und die Fördereinrichtung und/oder die Mischeinrichtung gemeinsam, insbesondere mittels ein und desselben, vorzugsweise steuerbaren, Antriebs in Rotation versetzbar sein, wobei sie beispielsweise auf ein und derselben Welle sitzen, welche den Homogenisator in Axialrichtung durchsetzt. Sofern gewünscht, kann im Falle des Vorhandenseins einer Fördereinrichtung der Rotor von dem Antrieb entkoppelbar sein, um das Produkt bedarfsweise bei ruhendem Rotor völlig frei von durch den Rotor induzierten Scherkräften durch den Homogenisator hindurch fördern zu können. Entsprechendes kann für die Mischeinrichtung gelten, sofern es z.B. erwünscht ist, die fließfähigen Stoffe bei ruhendem Rotor und ruhender Mischeinrichtung lediglich mittels der Fördereinrichtung durch den Homogenisator zu fördern, um sie langsam und schonend zu mischen bzw. zu homogenisieren.In order to provide a structurally very simple and cost-effective design, the rotor and the conveyor and / or the mixing device can be set in rotation, in particular by means of one and the same, preferably controllable, drive, for example, sit on one and the same shaft, which passes through the homogenizer in the axial direction. If desired, in the case of the presence of a conveyor, the rotor may be decoupled from the drive in order to be able to convey the product, if necessary, with rotor at rest completely free of shear induced by the rotor through the homogenizer. The same can apply to the mixing device, provided that e.g. it is desirable to promote the flowable materials with a stationary rotor and stationary mixing device only by means of the conveyor through the homogenizer to mix them slowly and gently or homogenize.
Alternativ können einerseits der Rotor, andererseits die Fördereinrichtung und gegebenenfalls auch die Mischeinrichtung, im letztgenannten Fall vorzugsweise die Fördereinrichtung gemeinsam mit der Mischeinrichtung, selbstverständlich auch unabhängig voneinander angetrieben sein.Alternatively, on the one hand, the rotor, on the other hand, the conveyor and possibly also the mixing device, in the latter case preferably the conveyor together with the mixing device, of course, be driven independently.
Der Rotor und der Stator können im wesentlichen die Form eines Zylindermantels mit hierin freigelassenen, in Umfangsrichtung verteilt angeordneten, radialen Öffnungen besitzen, wobei zwischen dem Rotor und dem in einer ersten Position befindlichen Stator der Scherspalt gebildet ist. Der Rotor kann selbstverständlich eines oder mehrere Rotorblätter umfassen, wie beispielsweise zwei Rotorblätter, von welchen eines radial innerhalb und eines radial außerhalb des Stators angeordnet ist, so daß bei dem in einer ersten Position befindlichen Stator zwei Scherspalte gebildet sind, wobei die einzelnen Rotorblätter wiederum gemeinsam oder getrennt voneinander angetrieben sein können oder einzeln oder gemeinsam von einem jeweiligen oder gemeinsamen Antrieb entkoppelbar sein können. Die radialen Öffnungen des Rotors können in jedem Fall vorzugsweise eine verschiedene Form und/oder Größe wie die Öffnungen des Stators besitzen.The rotor and the stator may be substantially in the form of a cylinder jacket having circumferentially distributed radial openings exposed therein, with the shear gap formed between the rotor and the stator in a first position. The rotor may, of course, comprise one or more rotor blades, such as two rotor blades, one of which is disposed radially inward and radially outward of the stator, so that in a first rotor Position of the stator two shear gaps are formed, wherein the individual rotor blades may in turn be driven together or separately from each other or may be individually or jointly decoupled from a respective or common drive. In any case, the radial openings of the rotor may preferably have a different shape and / or size than the openings of the stator.
Während der Stator grundsätzlich auch manuell in Bezug auf den Rotor verlagerbar sein kann, sieht eine vorteilhafte Ausgestaltung vor, daß zur Verlagerung des Stators in Bezug auf den Rotor ein Stellantrieb vorgesehen ist. Hierfür kommen praktisch beliebige bekannte, insbesondere in Form von Linearantrieben ausgebildete Stellantriebe in Betracht, wie beispielsweise hydraulisch, pneumatisch oder hydropneumatisch betätigte Kolben-/Zylindereinheiten, mechanisch oder gleichfalls fluidisch betätigte Schubstangen, Zahnstangen, Schraubengewinde etc. Der Stellantrieb kann in jedem Fall vorzugsweise bei rotierendem Rotor betätigbar sein.While the stator can basically also be displaced manually relative to the rotor, an advantageous embodiment provides that an actuator is provided for displacing the stator with respect to the rotor. For this purpose, virtually any known, designed in particular in the form of linear actuators actuators into consideration, such as hydraulically, pneumatically or hydropneumatically actuated piston / cylinder units, mechanically or equally fluidly actuated push rods, racks, screw thread, etc. The actuator can in each case preferably with rotating Rotor be actuated.
In weiterhin vorteilhafter Ausgestaltung kann vorgesehen sein, daß der Stellantrieb an einem das Gehäuse des Homogenisators stirnseitig verschließenden Deckel festgelegt ist, wobei der Deckel mit dem Stellantrieb insbesondere von dem Gehäuse des Homogenisators abnehmbar und gegen einen mit einer stirnseitigen Einlaßöffnung zur Aufgabe einer zusätzlichen Stoffkomponente versehenen Deckel auswechselbar sein kann. Letztere Ausführungsvariante eröffnet dem erfindungsgemäßen Homogenisator eine weitere Anwendung, nämlich das Eindispergieren einer weiteren Stoffkomponente über den zusätzlichen Einlaß in den fließfähigen Stoff, wobei die zusätzliche Stoffkomponente insbesondere pulver- oder partikelförmig sein kann. Infolge des durch den rotierenden Rotor bewirkten Unterdruckes kann die zusätzliche Stoffkomponente auf einfache Weise eingesaugt und in den Stoff eindispergiert werden, wobei ein Verklumpen auch im Falle von sehr feinpartikulären Stoffkomponenten vermieden wird, weil die Stoffkomponenten in dem Bereich des Homogenisators mit sehr hohen Turbulenzen, d.h. im Bereich des Rotor-/Statorsystems, zusammengeführt werden.In a further advantageous embodiment can be provided that the actuator is fixed to a cover of the housing of the homogenizer frontally closing, the cover with the actuator in particular from the housing of the homogenizer and removable against a provided with an end inlet opening for the task of an additional substance component lid can be interchangeable. The latter embodiment opens up a further application to the homogenizer according to the invention, namely the dispersing of a further substance component via the additional inlet into the flowable substance, wherein the additional substance component is in particular powdery or particulate can be. As a result of the negative pressure caused by the rotating rotor, the additional substance component can be easily sucked in and dispersed into the substance, whereby lumping is avoided even in the case of very fine particulate matter components, because the substance components in the region of the homogenizer with very high turbulence, ie in the area of the rotor / stator system.
Im Hinblick auf eine einfache und schnelle bedarfsweise Umrüstung des Homogenisators kann der Stellantrieb insbesondere gemeinsam mit dem hieran axial verlagerbar angeordneten Stator abnehmbar sein, wobei an dem mit einer stirnseitigen Einlaßöffnung versehenen Deckel ein Stator fest angeordnet sein kann, von welchem in der Montageposition des Deckels zumindest ein axialer Abschnitt unter Bildung des Scherspaltes radial neben dem Rotor angeordnet ist, so daß bei der Montage des mit dem zusätzlichen Einlaß versehenen Deckels automatisch ein Stator in einer ersten Position angeordnet ist und auf die eingesaugte weitere Stoffkomponente folglich sogleich sehr hohe Scherkräfte wirken, um für eine homogene Eindispergierung derselben, gegebenenfalls unter mechanischer Zerkleinerung, zu sorgen. Sofern eine demgegenüber schonendere Eindispergierung erwünscht ist, z.B. im Falle von gegenüber mechanischer Einwirkung empfindlichen Stoffkomponenten, kann der Deckel selbstverständlich auch nicht mit einem Stator ausgestattet sein, oder der Stator kann insbesondere lösbar an dem mit dem zusätzlichen Einlaß versehenen Deckel befestig sein, um ihn bedarfsweise abnehmen bzw. aufsetzen zu können. Letzteres kann hinsichtlich einer einfachen und schnellen Montage vorzugsweise mittels eines Schnellverschlusses, wie einer Rastverbindung, geschehen.With a view to a simple and rapid conversion of the homogenizer as needed, the actuator can be removed in particular together with the stator axially displaceable thereon, wherein on the provided with a frontal inlet opening a stator can be fixed, of which in the mounting position of the lid at least an axial section to form the shear gap is arranged radially adjacent to the rotor, so that during assembly of the cover provided with the additional inlet, a stator is automatically arranged in a first position and consequently immediately act on the sucked further material component very high shear forces to a homogeneous Eindispergierung same, optionally with mechanical comminution to provide. If, on the other hand, a more gentle dispersion of dispersion is desired, for example in the case of material components which are sensitive to mechanical action, the cover can of course not be equipped with a stator, or the stator can in particular be fastened detachably to the cover provided with the additional inlet in order to be able to do so to be able to remove or put on. The latter can be done with respect to a simple and quick installation, preferably by means of a quick release, such as a latching connection.
Alternativ oder zusätzlich kann selbstverständlich auch vorgesehen sein, daß das Gehäuse, z.B. an der dem Einlaß entgegengesetzten Seite des Rotor-/Statorsystems oder auch an der diesem zugewandten Seite desselben, wenigstens einen zweiten Einlaß zur Aufgabe einer zusätzlichen Stoffkomponente aufweist, wobei ein solcher zweite Auslaß zweckmäßig mittels eines Absperrorgans verschließbar sein sollte. In diesem Fall kann durch Verstellen des Stators zwischen seiner ersten und zweiten Position beim Öffnen des Absperrorgans anläßlich eines gewünschten Eindispergierens einer weiteren Stoffkomponente wiederum für eine hohe Scherwirkung (mit dem in einer ersten Position befindlichen Stator) oder auch für eine sehr geringe Scherwirkung bis praktisch null (mit dem Stator in der zweiten Position) gesorgt werden.Alternatively or additionally, it may of course also be provided that the housing, e.g. at the inlet opposite side of the rotor / stator system or on the side facing the same, at least one second inlet for the task of an additional substance component, wherein such a second outlet should be suitably closed by means of a shut-off. In this case, by adjusting the stator between its first and second position when opening the obturator on the occasion of a desired dispersing a further material component in turn for a high shear (with the located in a first position stator) or for a very low shear to practically zero (with the stator in the second position) are taken care of.
Weitere Merkmale und Vorteile der Erfindung ergeben sich aus der nachfolgenden Beschreibung eines Ausführungsbeispiels unter Bezugnahme auf die Zeichnungen. Dabei zeigen:
- Fig. 1
- eine perspektivische Ansicht einer Ausführungs- form eines erfindungsgemäßen Homogenisators in teilweise geschnittener Darstellung;
- Fig. 2
- einen Längsschnitt durch den Homogenisator gemäß
Fig. 1 ; - Fig. 3
- eine perspektivische Explosionsdarstellung des Rotor-/Statorsystems des Homogenisators gemäß
Fig. 1 und 2 einschließlich seiner Förder- und Mischeinrichtung sowie des Stellantriebs seines Stators; und - Fig. 4
- eine der
Fig. 3 entsprechende Explosionsdarstel- lung des Homogenisators gemäßFig. 1 , wobei ein den Stellantrieb tragender Gehäusedeckel ge- gen einen mit einer stirnseitigen Einlaßöffnung zur Aufgabe einer zusätzlichen Stoffkomponente versehenen Deckel ausgetauscht worden ist.bis 3
- Fig. 1
- a perspective view of an embodiment of a homogenizer according to the invention in a partially sectioned representation;
- Fig. 2
- a longitudinal section through the homogenizer according to
Fig. 1 ; - Fig. 3
- an exploded perspective view of the rotor / stator system of the homogenizer according to
Fig. 1 and 2 including its conveying and mixing device and the actuator of its stator; and - Fig. 4
- one of the
Fig. 3 corresponding exploded view of the homogenizer according toFig. 1 to 3 in which a housing cover carrying the actuator has been replaced by a cover provided with an end inlet opening for discharging an additional substance component.
In
Der Homogenisator 1 kann beispielsweise Teil einer in
Wie insbesondere aus
Wie wiederum insbesondere der
Die Fördereinrichtung 25 weist, wie bereits oben angedeutet, etwa schneckenförmige Förderelemente 26 auf, welche sich um zumindest einen Abschnitt des Umfangs ihrer Drehachse, d.h. der Welle 12, und von dort bis in den Bereich der sie umgebenden Innenwand des Gehäuses 2 unter Freilassung eines nur schmalen Spaltes von beispielsweise etwa 0,5 mm erstrecken. Die Innenwand des Gehäuses 2 verengt sich (in Förderrichtung betrachtet) im Bereich der Förderelemente 26 zum Zwecke eines geeigneten Druckaufbaus in dem Homogenisator 1, wobei das freie - umfangsseitige- Ende der Förderelemente 26 z.B. gemäß der Verjüngung der Innenwand des Gehäuses 2 mit einer Abschrägung versehen sein kann (vgl.
Der Stator 17 befindet sich, wie bereits angedeutet, in der in
Wie weiterhin insbesondere den
Um dem Homogenisator 1 eine weitere Anwendung, nämlich das Eindispergieren einer zusätzlichen Stoffkomponente unter zuverlässiger Vermeidung eines Verklumpens auch sehr feinpartikulärer Stoffe, zu eröffnen, ist beim vorliegenden Ausführungsbeispiel der Deckel 33 mit dem Stellantrieb 30 von dem Gehäuse 2 abnehmbar und gegen einen in der
Der Homogenisator 1 gemäß
Im "Schermodus" befindet sich der Stator 17 in der in
Im "Pumpmodus" befindet sich der Stator 17 aus der in
Claims (18)
- A homogeniser (1) for homogenising or dispersing fluid substances, having a shaft (12) which supports a rotor (16), the shaft (12) being rotatably supported and being rotably driven by means of a drive that is, in particular, controllable, and having a stator (17) that interacts with the rotor (16), wherein at least one shear gap is formed between the rotor (16) and the stator (17), characterised in that the stator (17) is axially displaceable in relation to the rotor (16) between at least one first position, in which at least one axial section of the rotor (17) is arranged radially adjacent to the rotor (16) with the formation of the shear gap, and a second position in which the stator (17) is arranged adjacent to the rotor (16) in the axial direction, so that a shear gap is no longer present between the rotor (16) and stator (17).
- The homogeniser according to Claim 1, characterised in that the stator (17) is arranged in the second position with an axial distance from the rotor (16), wherein the stator (17), particularly in the second position, abuts against a stop arranged on the side of the stator (17) facing away from the rotor (16).
- The homogeniser according to Claim 1 or 2, characterised in that the stator (17), in at least one first position, is arranged radially adjacent to the rotor (16) essentially along its entire axial extension.
- The homogeniser according to any one of Claims 1 to 3, characterised in that- the stator (17) is displaceable exclusively between a first position and the second position in relation to the rotor (16); or in that- the stator (17) is also displaceable relative to the rotor (16) between a plurality of first positions in which the stator (17) is in each case arranged radially adjacent to the rotor (16) at least with an axial section.
- The homogeniser according to any one of Claims 1 to 4, characterised in that the rotor (16) is arranged in axially fixed manner and the rotor (17) is displaceable in the axial direction.
- The homogeniser according to any one of Claims 1 to 5, characterised in that a conveying device (25) is arranged before the rotor/stator system formed from rotor (16) and stator (17).
- The homogeniser according to any one of Claims 1 to 6, characterised in that the rotor/stator system (16, 17) and, if necessary, the conveying device (25), are accommodated in a housing (2) in which is mounted the shaft (12) supporting the rotor (16), wherein the housing (2), in particular,- has at least one inlet (4) arranged upstream from the rotor/stator system (16, 17), which inlet is connectable, in particular, to a branch pipe of a tank equipped, in particular, with an agitator; and/or- has at least one outlet (5) arranged downstream from the rotor/stator system (16, 17), which outlet is connectable, in particular, to a return pipe of a tank equipped, in particular, with an agitator.
- The homogeniser according to Claim 7, characterised in that the outlet (5) of the housing (2) is arranged radially relative to the shaft (12) supporting the rotor (16) and in the axial region of the rotor/stator system (16, 17).
- The homogeniser according to any one of Claims 6 to 8, characterised in that the conveying device (25) has at least one conveying element (26) displaceable coaxially with the shaft (12) of the rotor (16), wherein the conveying device (25) is arranged, in particular, on a section of the housing (2) which reduces in width on the inside - viewed in the direction of conveying.
- The homogeniser according to any one of Claims 1 to 9, characterised in that it also has a mixing device (15), wherein the mixing device (15) has, in particular, at least one or more mixing blades (14) displaceable rotatably and coaxially with the shaft (12) of the rotor (16).
- The homogeniser according to any one of Claims 6 to 10, characterised in that- the rotor (16) and the conveying device (25) and/or the mixing device (15) are commonly rotatably displaceable, in particular by means of one and the same drive, wherein the rotor (16) and/or, if necessary, the mixing device (15) is/are, in particular, disconnectable from the drive; or in that- the rotor (16) on the one hand, the conveying device (25) on the other and, if necessary, the mixing device (15), are driven independently of each other.
- The homogeniser according to any one of Claims 1 to 11, characterised in that the rotor (16) and the stator (17) have essentially the shape of a cylinder jacket with radial openings or slots (21, 22, 23) let into the jacket and arranged so that they are distributed in the circumferential direction, wherein the radial openings (21, 22) of the rotor (16) have, in particular, a different shape and/or size from the openings (23) of the rotor (17).
- The homogeniser according to any one of Claims 1 to 12, characterised in that an actuator (30) is provided for displacing the stator (17) relative to the rotor (16), which actuator can be actuated, in particular, whilst the rotor (16) is rotating, wherein the actuator (30) is fastened, in particular, on a cover (33) sealing the housing (2) of the homogeniser (1) on the front side.
- The homogeniser according to Claim 13, characterised in that the cover (33) with the actuator (30) can be removed from the housing (2) of the homogeniser (1) and can be replaced by a cover (40) provided with a front-side inlet opening (41) for feeding an additional substance component, wherein the actuator (30) can, in particular, be removed together with the stator (17) axially displaceable thereon.
- The homogeniser according to Claim 14, characterised in that a stator (17b) is fixedly arranged on the cover (40) provided with a front-side inlet opening (41), of which, in the mounting position of the cover (40), at least one axial section is arranged with the formation of the shear gap radially adjacent to the rotor (16).
- The homogeniser according to any one of Claims 7 to 15, characterised in that the housing (2) has at least one second inlet (4a, 41) for feeding an additional substance component, wherein the second inlet (4a, 41) is sealable, in particular, by means of a shutoff mechanism.
- A homogenising device for homogenising or dispersing fluid substances, with a tank equipped, in particular, with an agitator and with at least one branch pipe branching from the tank and leading into an inlet (4) of a homogeniser (1), characterised by a homogeniser (1) according to any one of Claims 1 to 16.
- The homogenising device according to Claim 17, characterised in that at least one outlet (5) of the homogeniser (1) opens into the tank by means of a return pipe.
Priority Applications (1)
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PL10011599T PL2305370T3 (en) | 2009-09-30 | 2010-09-29 | Homogeniser and homogenising device with such a homogeniser |
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DE102009047777A DE102009047777A1 (en) | 2009-09-30 | 2009-09-30 | Homogenizer and homogenizer with such a homogenizer |
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AT (1) | ATE556765T1 (en) |
DE (1) | DE102009047777A1 (en) |
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ES (1) | ES2386969T3 (en) |
PL (1) | PL2305370T3 (en) |
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Publication number | Priority date | Publication date | Assignee | Title |
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GB2536502A (en) * | 2015-03-20 | 2016-09-21 | Silverson Machines Ltd | Apparatus and method for high-shear mixing |
DE202018102804U1 (en) * | 2018-05-18 | 2019-08-22 | Symex Gmbh & Co. Kg | Device for homogenizing flowable substances |
WO2023156843A1 (en) * | 2022-02-15 | 2023-08-24 | CHALAMALASETTI, Vijay C.S Anand | An equipment for homogenization of fluids and a method for operating the same |
CN114939357B (en) * | 2022-06-24 | 2023-06-20 | 三一技术装备有限公司 | Bidirectional homogenizing equipment, pulping system and battery production system |
WO2024100447A2 (en) | 2022-11-07 | 2024-05-16 | Frymakoruma Ag | Homogeniser and vacuum process plant, and method using same |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DK174688B1 (en) | 2001-06-12 | 2003-09-15 | Scanima As | Homogenizing machine for the treatment of products to be homogenized, especially foodstuffs containing dairy products |
EP0620039A1 (en) * | 1993-04-15 | 1994-10-19 | KORUMA MASCHINENBAU GmbH | Homogenising device or similar |
DE9305553U1 (en) * | 1993-04-15 | 1993-05-19 | Koruma Maschinenbau Gmbh, 7844 Neuenburg | Homogenizing device or similar |
DE29608712U1 (en) | 1996-05-14 | 1996-09-05 | Wittek Axel | Homogenizer |
NL1008622C2 (en) * | 1998-03-17 | 1999-09-27 | Marfil Machinery B V | Mixing apparatus with agitator comprising impeller and variable cross section impeller cage |
DE20002920U1 (en) | 2000-02-18 | 2000-04-20 | Schröder & Boos Misch- und Anlagentechnik GmbH & Co. KG, 27578 Bremerhaven | Homogenizer |
DE10204923C1 (en) | 2002-02-07 | 2003-07-24 | Romaco Ag Frymakoruma Rheinfel | Sonotrode disperser, e.g. for cleaning applications, has radial bridges connecting central receptor shaft to cylindrical body |
DE10204921C1 (en) | 2002-02-07 | 2003-10-16 | Romaco Ag Frymakoruma Rheinfel | Dispersing apparatus |
DE20214291U1 (en) | 2002-09-14 | 2003-01-02 | Romaco Ag Frymakoruma Rheinfel | Mixer assembly, for viscous substances, has venturi mixer paddles on vertical rotating shaft |
DE20320052U1 (en) | 2003-12-24 | 2004-05-27 | Romaco Ag Frymakoruma | Device for milling solid particles and other substances has rotor and stator each constructed as disc with opposed milling faces, whereby substances for milling are movable in radial direction of opposed rotor and stator discs |
DE202005002002U1 (en) | 2005-02-09 | 2005-05-12 | Romaco Ag Frymakoruma | Device for homogenizing and/or dispersing flowable substance comprises return line having one end with switch provided in further return line and arranged in lower region of container |
DE202005018432U1 (en) | 2005-11-23 | 2006-08-24 | Frymakoruma Ag | Homogenizer for viscous fluids has a central feed to two rotating concentric toothed profile rings and with flow guides to increase fluid pressure and prevent cavitation |
DE202006008820U1 (en) | 2006-06-03 | 2006-08-17 | Frymakoruma Ag | Apparatus for dispersing and/or homogenizing liquids comprises processing unit comprising two independently rotating concentric toothed wheels driven on horizontal shafts |
WO2010099767A1 (en) | 2009-03-06 | 2010-09-10 | Frymakoruma Ag | Comminuting and dispersing apparatus |
-
2009
- 2009-09-30 DE DE102009047777A patent/DE102009047777A1/en not_active Withdrawn
-
2010
- 2010-09-29 DK DK10011599.7T patent/DK2305370T3/en active
- 2010-09-29 PL PL10011599T patent/PL2305370T3/en unknown
- 2010-09-29 ES ES10011599T patent/ES2386969T3/en active Active
- 2010-09-29 EP EP10011599A patent/EP2305370B1/en active Active
- 2010-09-29 AT AT10011599T patent/ATE556765T1/en active
Also Published As
Publication number | Publication date |
---|---|
ATE556765T1 (en) | 2012-05-15 |
DE102009047777A1 (en) | 2011-04-07 |
DK2305370T3 (en) | 2012-07-30 |
PL2305370T3 (en) | 2012-10-31 |
EP2305370A1 (en) | 2011-04-06 |
ES2386969T3 (en) | 2012-09-07 |
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