CN1803267A - Stirring and mixing device - Google Patents
Stirring and mixing device Download PDFInfo
- Publication number
- CN1803267A CN1803267A CN 200510129550 CN200510129550A CN1803267A CN 1803267 A CN1803267 A CN 1803267A CN 200510129550 CN200510129550 CN 200510129550 CN 200510129550 A CN200510129550 A CN 200510129550A CN 1803267 A CN1803267 A CN 1803267A
- Authority
- CN
- China
- Prior art keywords
- powder
- stirring
- mixing arrangement
- housing
- inlet tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Landscapes
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
A stirring and mixing device 110 comprises an introduction pipe 55 which is provided with a powder introduction port 24 and a liquid introduction port 22 , an extrusion pipe 60 which is connected to the introduction pipe 55 and extrudes a mixture of powder and liquid introduced through the introduction pipe 55 to its one end portion, a casing 12 which is connected to one end portion of the extrusion pipe 60 and provided with a passage through which a fluid of the extruded mixture is made to flow, and a stirrer 15 which is disposed within the casing 12 and comprised of a shaft portion 14 connected to a drive source 20 and a stirring blade 16 attached to the external surface of the shaft portion 14 . A funnel-shaped powder introducing device 57 is attached to the powder introduction port 24 , a feeder 54 for conveying powder is disposed in the powder introducing device 57 , and the feeder 54 is connected to an oscillatory rotation drive source 53.
Description
Coherent reference
Here the whole contents of Japanese patent application No.2004-354736 and 2005-219673 comprises explanation, claims, and figure and summary are with their full text, and be as a reference incorporated.
Technical field
The present invention relates to a kind of stirring and mixing arrangement, it carries powder that powder is introduced by making a feed appliance with mode of oscillation rotation, and stirs and mix with liquid.
Background technology
For example, known add liquid with powder, add powder to mix with liquid, and add simultaneously under liquid and the situation of powder their mixing, in liquid, can produce the particle (so-called undissolved agglomerate) of the secondary gathering of powder, and, more formed secondary aggregation is dispersed in the liquid quite difficult.In addition, the secondary aggregation stops up raw material inlet, is easy to cause powder afterwards to introduce the very situation of difficult that becomes.
Therefore, the apparatus and method that the secondary aggregation occurs have been proposed when mixed-powder and liquid, can suppress recently.
Japanese Patent Laid-Open Publication No.Hei 11-19495, No.2001-62273 and No.2002-166154 have proposed a kind of continuous mixing arrangement that is used for liquid and powder, a rotating disc wherein is set in a housing, this housing is provided with a superposed supply opening and a floss hole that is positioned at the bottom that is used for liquid and powder, housing is divided into one goes up stirring chamber and a following stirring chamber, a scraper is installed to the top of rotating disc, and with the scraper of a rotation be installed in rotating disc below, the scraper of this rotation is to rotate independently with the discontiguous state of rotating disc, by rotating disc is rotated the powder and the liquid of discharging by supply opening are mixed mutually, and, the rotation scraper mixes the mixture that moves to down stirring chamber, and these mixtures are carried out scraping, the velocity of rotation of this rotation scraper is lower than the speed of rotating disc, and makes mixture discharge by floss hole continuously.
Japanese Patent Laid-Open Publication No.2002-248330 and No.2001-198447 advise a kind of continuous mixing arrangement, by means of the mixing pan mixed-powder and the liquid of a rotation, wherein, supply liquid by spray, and powder is mixed equably with liquid.
Japanese Patent Laid-Open Publication No.2001-65850 proposes the method for a kind of mixed-powder such as coal dust and flowing fluid ratio such as water, prepare a kind of mud, this method comprises helicoidal pump of powders into, mid point supply water by this helicoidal pump, powder is mixed with liquid, rising pressure, and reduce pressure at the floss hole of helicoidal pump, form mud.
In addition, the inventor has proposed a kind of dissemination apparatus in Japanese Patent Laid-Open Publication No.2000-246131 kind, it has and is used for a housing of adorning two or more materials therein and a rubber that is arranged in this housing, wherein, form irregular position at least one surface in the outer surface of the inner surface of housing and rubber, make the relative to each other reciprocally motion of housing and rubber, and be used in the compression pressure that produces in the gap between the outer surface of the inner surface of housing and rubber and be dispersed at least a material in two or more materials.
Yet, do not have in above-mentioned mixing arrangement and the mixed method a kind of can be by not allowing the secondary aggregation occur preventing that the powder intake is blocked fully, and the powder that can mix and the combination of liquid are restricted.
According to above-described mixing arrangement and mixed method, when mixing by liquid, dissolving, chemical reaction, polymerisation, when perhaps similar procedure acquisition material and liquid had very high viscosity, existence mixes can not sufficiently uniform possibility.
Specifically, powder and liquid near the powder inlet port, mutually combine that part of, liquid contacts directly or indirectly with powder near the powder inlet port.Therefore, powder absorbs moisture near the powder inlet port, produces the secondary aggregation, may cause the obstruction of powder inlet port.In addition, proceed to stir and the operation that mixes becomes very difficult.
Therefore, the invention provides a kind of stirring and mixing arrangement, it is suppressed at the appearance of secondary aggregation in powder and the liquid cohesive process, prevent that raw material inlet from being stopped up by the secondary aggregation, it has versatility widely, for the combination of the combination of liquid that will mix and liquid and powder and liquid basically without limits, and is mixed with the even of liquid with liquid and powder by liquid, the angle of reaction and similar procedure sees that it has fabulous performance.
Summary of the invention
Stirring of the present invention and mixing arrangement have following characteristics:
(1) this stirring and mixing arrangement have an inlet tube, it is provided with a powder intake, at least one is arranged near the following liquid intake of powder intake, carry the feed appliance of powder and powder and mixtures of liquids, and a rotary driving source that makes the vibration that feed appliance rotates in vibration (or concussion) mode.
The liquid intake be arranged near the powder intake below, make the powder of introducing to spread out, and successfully to the whereabouts.
(2) in the stirring of describing in superincumbent (1) and mixing arrangement, feed appliance is at least in the position of liquid intake or be provided with the helical blade of carrying powder below the position of liquid intake, and the size of the helical blade of this conveying powder makes its side partly reach near the madial wall of inlet tube.
The helical blade of this conveying powder can successfully be carried powder downwards, and can not interrupt the flow of powder in inlet tube.
(3) in the stirring of describing in superincumbent (1) or (2) and mixing arrangement, feed appliance is provided with at least one cut-off blade, is used for cutting powder and mixtures of liquids.
This cut-off blade makes that by mixture being cut into suitable size waltzing through inlet tube carries mixture to become possibility.
(4) superincumbent (1) in any one described stirring and the mixing arrangement, also is provided with an overfall in (3) below the powder intake and above the liquid intake.
Even powder introducing amount and/or liquid introducing amount surpass the conveying capacity of inlet tube, there are not powder and mixtures of liquids to overflow, by the possibility of powder intake toward backflow yet.Therefore, prevented that the mixed thing of powder intake from stopping up, and can with stable manner powder have been introduced continuously.
(5) Shang Mian (1) any one described stirring and mixing arrangement in (4) also comprises an extruded tube, a housing and an agitator, extruded tube is connected on the inlet tube, and this extruded tube is expressed to an end parts to powder and the mixtures of liquids introduced by inlet tube; Housing is connected on the end parts of extruded tube, and this housing is provided with a passage, makes the mixture fluid that is extruded by this channel flow; And agitator is arranged in the housing, and this agitator comprises the stirring vane on the outer surface that is connected to a shaft portion on the oscillation source and is attached to this shaft portion.
That crosses as described above is such, because the rotation of feed appliance vibration, even the liquid of introducing is contacting with powder near the powder intake and owing to powder with because the secondary of liquid adheres on the feed appliance near assembling the powder intake of deposit at inlet tube that is produced, also these deposits can removed by feed appliance.In addition, rotate and by the powder intake secondary aggregation to be introduced in the inlet tube at any time or continuously by the vibration of feed appliance.Therefore, the agglomerate that can prevent the secondary aggregation is along with the time increases its size, and can prevent that the powder intake from being stopped up by very large secondary aggregation.In addition, squeeze in the housing by extruded tube by the powder of inlet tube introducing and the aggregation of mixtures of liquids, thereby mixture can be delivered in the housing at any time or continuously, and can not deposit, subsequently mixture be stirred and mix.Therefore, can obtain not have the fluid of the homogeneous mixture of secondary aggregation.
(6) in the stirring of describing in superincumbent (5) and mixing arrangement, feed appliance comprises that also the first axle part divides and the second axle part branch, and the rotary driving source of vibration comprises that one is used for making the first axle part to divide ROTATING SOURCE and an oscillation source that is used for making the vibration of the second axle part branch of rotation.
(7) in the stirring of describing in superincumbent (5) or (6) and mixing arrangement, by passage separately being provided with at least one stirring chamber in housing with distribution plate.
Cause turbulent flow in the passage that is arranged on housing of distribution plate, further improved stirring efficiency.
(8) superincumbent (5) in any one described stirring and the mixing arrangement, housing also is provided with a floss hole in (7), and, be used for the filter that the content in the housing filters is arranged near this floss hole.
This filter be arranged so that material by the dissolving of undissolved material and unnecessary filtration of material being fallen to obtain want, mixture, reactant, perhaps analog becomes possibility.
(9) Shang Mian (5) any one described stirring and mixing arrangement in (9) also comprises at least one steam intake, by it steam is incorporated in the housing.
(10) superincumbent (5) in (9) in any one described stirring and the mixing arrangement, the pressure by adjusting vapor volume and/or steam is to being introduced into mixture in the housing and heating and/or dissolve and/or sterilizing.
(11) superincumbent (5) in (10) in any one described stirring and the mixing arrangement, the viscosity or the reaction of the pressure adjusting mixture by regulating vapor volume and/or steam.
(12) Shang Mian (5) any one described stirring and mixing arrangement in (11) also comprises at least one liquid intake, inserts the liquid in the housing by it.
Be used for being arranged so that of liquid intake that liquid is introduced in the housing diluted the mixture of introducing in the housing, viscosity and its reaction of adjusting of regulating it become possibility.
(13) in the stirring and mixing arrangement described in superincumbent (12), regulate the viscosity or the reaction of mixture by regulating the amount of liquid of introducing.
Description of drawings
To be basic the preferred embodiment of the present invention will be described in detail with following figure, wherein:
Fig. 1 is the cutaway view of a cardinal principle, shows an example according to the structure of stirring of the present invention and mixing arrangement;
Fig. 2 is the cutaway view of a cardinal principle, shows the structure of the drive source of the feed appliance that is connected to stirring shown in Figure 1 and the powder introducing device on the mixing arrangement;
Fig. 3 is the cutaway view of a cardinal principle, shows the structure of another drive source of the feed appliance that is connected to stirring shown in Figure 1 and the powder introducing device on the mixing arrangement;
Fig. 4 is the cutaway view of a cardinal principle, shows the structure of another drive source of the feed appliance that is connected to stirring shown in Figure 1 and the powder introducing device on the mixing arrangement;
Fig. 5 is the cutaway view of a cardinal principle, shows the structure of another drive source of the feed appliance that is connected to stirring shown in Figure 1 and the powder introducing device on the mixing arrangement;
Fig. 6 is a schematic cutaway view, shows the structure of another embodiment of the inlet tube of the powder of stirring shown in Fig. 1 and mixing arrangement and liquid;
Fig. 7 is the cutaway view that the line A-A ' along Fig. 6 gets;
Fig. 8 is a schematic diagram, shows the another kind of structure of feed appliance in the structure of the inlet tube shown in Fig. 6;
Fig. 9 is a schematic diagram, shows another structure of feed appliance in the structure of the inlet tube shown in Fig. 6; And
Figure 10 is a schematic diagram, shows another structure of feed appliance in the structure of the inlet tube shown in Fig. 6.
The specific embodiment
Referring now to accompanying drawing the preferred embodiments of the present invention are described.
The structure of an example of stirring of the present invention and mixing arrangement will be described with reference to figure 1.
Stirring and mixing arrangement 110 have an inlet tube 55, an extruded tube 60, a housing 12 and an agitator 15, this inlet tube 55 is provided with a powder intake 24 and a liquid intake 22, extruded tube 60 is connected to inlet tube 55, an and end parts that will be expressed to it by the powder and the mixtures of liquids of inlet tube 55 introducings, housing 12 is connected on the end parts of extruded tube 60, and this housing is provided with a passage, the fluid of the feasible mixture that is extruded is by this channel flow, and agitator 15 is arranged in the housing 12, and this agitator comprise be connected to one on the drive source 20 shaft portion 14 and be attached to stirring vane 16 on the outer surface of this shaft portion 14.A funnel shaped powder introducing device 57 is attached on the powder intake 24, and one is used for carrying the feed appliance 54 of powder to be arranged on this powder introducing device 57, and feed appliance 54 is connected on the rotary driving source 53 of a vibration.
To the structure of stirring and mixing arrangement 110 be described in more detail.
As mentioned above, inlet tube 55 is provided with a powder intake 24 and a liquid intake 22.A fluid storage jar 76 is connected on the liquid intake 22 by valve 72 and pump 74, and mixing material 78 is stored in this fluid storage jar 76.Funnel shaped powder introducing device 57 is connected on the powder intake 24, and the funnel shaped floss hole of powder introducing device 57 is stretched out, thereby inserts in the inlet tube 55.Here, preferably powder intake 24 and liquid intake 22 are closed each other.Therefore, can be with the ratio of a regulation at any time or continuously mixed-powder and liquid.Powder introducing device 57 is provided with the feed appliance 54 that is used for carrying powder, and this feed appliance is connected on the source of rotational drive 53 of vibration.The source of rotational drive 53 of vibration is described to Fig. 5 below with reference to Fig. 2.
Fig. 1 shows the configuration of inlet tube 55 and powder introducing device 57 made and is separated from each other, but is not limited to such configuration.For example, can with make in the configuration of inlet tube shown in Fig. 1 55 and powder introducing device 57 as at Fig. 6 to a body as shown in Fig. 9.Particularly, as shown in Figure 6, inlet tube 55 can be provided with a funnel shaped powder intake 17 on its top.Make feed appliance 54 be arranged on the top of funnel shaped powder intake 17 in order to the rotating part 53 of the vibration of conveying powder with the mode of oscillation rotation.Feed appliance 54 is provided with helical blade 11 and powder conveyor screw blade 52.Hope is provided with the position of liquid intake 22 at least with powder conveyor screw blade 52, perhaps be arranged on this intake below.In Fig. 1, feed appliance 54 also is provided with blade.Inlet tube 55 is provided with liquid intake 22 on its side surface.Cross as described above like that, preferably insert the liquid into mouthfuls 22 be arranged near the powder intake 17 below.Liquid intake 22 be arranged near the powder intake 17 below make powder fall to become possibility with liquid.Therefore, can improve powder and introduce efficient, and can prevent that powder from raising.
Figure 7 illustrates the profile of doing along the line A-A ' of Fig. 6.As shown in FIG. 7, four positions on the side surface of inlet tube 55 form liquid intake 22, but are not limited to this four positions.Preferably insert the liquid into mouth 22 and be arranged at least one and a plurality of positions, preferably in two or more positions respect to one another.Preferably, by liquid intake 22 liquid is sprayed into.
As shown in FIG. 8, can change pitch between the powder conveyor screw blade 52 that is located on the feed appliance 54 each.For example, can make its configuration as illustrated in Figure 8, make pitch between each powder conveyor screw blade 52 narrow near the position the liquid intake 22 by the powder discharge position of powder intake 17, thereby can introduce powder continuously, and make position that pitch between each the powder conveyor screw blade 52 powder and liquid below liquid intake 22 meets, thereby can carry powder and mixtures of liquids at any time downwards than broad.Therefore, can successfully carry powder and mixture simultaneously.
As shown in FIG. 9, a cut-off blade 51 can be set in the bottom of feed appliance 54.For example, near the cut-off blade that is provided with below liquid intake 22 51 makes that the mixture of the liquid of introducing by liquid intake 22 and the powder that just meets with the liquid of introducing is cut into suitable size becomes possibility.As a result, can successfully mixture be carried by inlet tube 55.When can forming the undissolved agglomerate of mixture, mixture has the velocity of rotation of higher vibration if the ROTATING SOURCE of vibration can be set for, the powder that will mix and the character of liquid are depended in the formation of the undissolved agglomerate of this formation, perhaps, if having the velocity of rotation of lower vibration when setting the ROTATING SOURCE of vibration for mixture mobile strong.
As shown in Figure 10, inlet tube 55 can be provided with overfall 13 below the powder intake 17 shown in Fig. 6 and above liquid intake 22.Even the quantity that quantity that powder is introduced and/or liquid are introduced above the conveying capacity of inlet tube, can prevent powder and mixtures of liquids overflow and reflux by the powder intake is past.In addition, can prevent the powder intake because mixture is blocked toward refluxing by the powder intake, thereby can with stable manner powder be introduced continuously.Even powder and mixtures of liquids are introduced in the extruded tube 60 by inlet tube 55 with the amount that surpasses the conveying capacity that is connected to the extruded tube 60 on the inlet tube 55 shown in Fig. 1, mixture is also determined without any the possibility that is back to the powder intake, and this is because inlet tube 55 is provided with overfall 13.Therefore, can prevent that the powder intake is blocked.
As shown in Figure 10, the size of the powder conveyor screw blade 52 of feed appliance 54 is formed, make its side partly reach near the madial wall of inlet tube 55.Therefore, powder and powder and mixtures of liquids can not be deposited on the madial wall of inlet tube 55, and the result can successfully carry powder and powder and mixtures of liquids continuously.
By flange 67 inlet tube 55 is connected on the extruded tube 60.In this embodiment, use a Mohno pump as extruded tube 60.Specifically, the rotor 61 that is connected to the external spiral shape on the motor 63 is arranged in the extruded tube 60.For example, can adopt " the NEMO of HEISHIN Ltd. company
Pump " as the Mohno pump.
By flange 65 extruded tube 60 is connected on the housing 12.Housing 12 is formed with a passage therein, and fluid is by this channel flow, and in housing 12, have agitator 15, this agitator to comprise to be connected to one on the drive source 20 shaft portion 14 and be attached to stirring vane 16 on the outer surface of this shaft portion 14.Stirring vane preferably has the shape of spiral, the shape of bar, and perhaps similar shape depends on that the raw material that will stir suitably selects.
In this embodiment, extruded tube 60 is connected to the upstream of housing 12.
At least one distribution plate 18 is set in housing 12 and passage, makes fluid or powder to flow continuously, and, the housing of being separated by distribution plate 18 12 has stirring chamber 200a, 200b, 200c, the mixtures that stirring extent is different are introduced in these chambers continuously.That crosses as described above is such, with distribution plate 18 inside of housing 12 is separated to have strengthened turbulence effect.Yet using distribution plate 18 is not necessity, if can stir at an easy rate and mix according to raw material properties, does not just need distribution plate 18.
Be provided with a steam intake 88 at the stirring chamber 200a of housing 12 middle and upper reaches, stirring chamber 200b is provided with a steam and introduces chamber 84, and, between steam introducing chamber 84 and passage, be provided with a filter 86.Steam is introduced chamber 84 and is provided with a steam intake 85, and steam is introduced in the housing 12 by filter 86 with the form of mist that desirable even volume is arranged.Steam intake 85,88 can be provided with a pressure gauge (not shown), is used for measuring the injection pressure of steam.Therefore, can regulate the volume and the pressure of steam.
As another embodiment, also can be the stirring chamber 200a of the housing 12 middle and upper reaches sides of describing in the above as the liquid intake.Equally, the liquid intake can be provided with a flowmeter (not shown), can measure the amount of the liquid that will introduce.The example of the liquid of introducing by the liquid intake comprises and the solvent of powder (for example water, alcohol), with the solvent of powdered reaction, and analog.Here, the solvent that is used to mix can be and the identical solvent of supplying by the liquid intake 22 of the inlet tube 55 shown in Fig. 1 of liquid, or a kind of different solvent.In the above embodiments, the stirring chamber 200b of housing 12 is provided with mode and introduces chamber 84 with top identical steam, this steam is introduced chamber 84 and is provided with steam intake 85, and steam is introduced in the housing 12 by filter 86 with the form of mist that desirable even volume is arranged.Steam intake 85 can be provided with a pressure gauge (not shown), is used for to measure the injection pressure of steam with top identical mode.Therefore, can regulate the volume of steam and the pressure of steam.
Stirring parts 200c is provided with a untreated material discharge mouth 64, and it also is provided with a filter 70 round agitator 15.Even in housing 12, have the undressed material (for example undissolved agglomerate) of raw material, only be merely able to by floss hole 64 untreated material discharge be gone out by means of filter 70.For example, can use the stainless steel or the ceramic filter spare of microgrid (fine mesh), reverse osmosis film, polymer film (nanofiltration film), perhaps similarity piece is used for filter 70.Filtered material is introduced in the treated chamber 82, and this chamber is arranged on the outside of the filter 70 of stirring chamber 200c, and treated chamber 82 is provided with the floss hole 62 of a material of handling.
Untreated material discharge mouth 64 is provided with a pressure gauge 80 and a vent valves 68, and treated material discharge mouth 62 is provided with a vent valves 66.
The rotary driving source 53 of vibration is described to Fig. 5 referring now to Fig. 2.
The rotary driving source 53 of vibration comprises to be made the rotating part that feed appliance 54 rotates and mainly makes the second axle part divide 48 oscillation sources that vibrate, as illustrated in Figure 2.
As shown in FIG. 2, ROTATING SOURCE comprises first gear 34, this gear is connected on the motor 36 as drive source, and this gear can rotate, ROTATING SOURCE also comprises second gear 32 and gear unit 30, this second gear 32 engages with first gear 34 and can rotate on the rotation direction opposite with first gear 34, and gear unit 30 has at second gear 32 on its outer wall and is connected to feed appliance 54 on its bottom.
Oscillation source has and is connected to the second axle part and divides a eccentric cam 50 on 48 the end, piston portion 40 and anti-rotation device, this piston portion 40 is connected to the second axle part and divides on 48 the other end, and be fitted in the gear unit 30, and anti-rotation device is arranged between piston portion 40 and the gear unit 30, and this device prevents from rotation is delivered on the piston portion 40.
The anti-rotation device of this embodiment comprises a journal bearing 42 and a thrust bearing 44, journal bearing 42 is arranged between the madial wall of the lateral wall of piston portion 40 and gear unit 30, and thrust bearing is arranged between the inside bottom of the bottom of piston portion 40 and gear unit 30 at least or between the apparent surface of the top of piston portion 40 and gear unit 30.Journal bearing 42 be arranged so that the rotation that prevents gear unit 30 is passed on the piston portion 40 and become possibility that wherein first gear 34 and second gear 32 are delivered to rotation on this gear unit 30.In addition, the setting of thrust bearing 44 can be so that first gear 34 engages with second gear 32, and rotation can be delivered on the gear unit 30, interrelating with the oscillating movement of piston portion 40 simultaneously makes gear unit 30 slide on the direction represented by arrow 102 at an easy rate, and wherein eccentric cam 50 makes piston portion 40 vibrations.
Except top configuration, the rotary driving source 53 of vibration can be configured to as illustrated in Figure 3.The rotary driving source of the vibration of Fig. 2 described above have between the inside bottom of the bottom that is arranged on piston portion 40 and gear unit 30 or between the apparent surface of the top of piston portion 40 and gear unit 30 in the thrust bearing 44 at least one position.Yet, being provided with dull and stereotyped 48a at the rotary driving source of the vibration shown in Fig. 3,48b replaces thrust bearing 44.
Dull and stereotyped 48a, 48b is arranged so that first gear 34 and second gear 32 are meshing with each other and becomes possibility rotation is delivered to gear unit 30, interrelating with the oscillating movement of piston portion 40 simultaneously makes gear unit 30 slide on the represented direction of arrow 102 at an easy rate, and wherein eccentric cam 50 makes piston portion 40 vibrations.
To be described in Fig. 2 now, the operation of the rotary driving source of the vibration shown in 3.
In the rotary driving source 53 of vibration, drive eccentric cam 50 and make the second axle part divide 48 on the represented direction of the arrow as shown in Fig. 2 or 3 108, to vibrate.Therefore, being connected to the second axle part divides the piston portion 40 on 48 to vibrate on the represented direction of arrow 102.
With the driving of eccentric cam 50 CD-ROM drive motor 36 simultaneously or dividually, so that first gear 34 rotates on the represented direction of arrow 100.Therefore, the rotation of first gear 34 is delivered on second gear 32 with 34 engagements of first gear, and second gear 32 is to rotate on the represented direction of arrow 104 in the direction with the direction of rotation of first gear 34.As a result, on the represented direction of arrow 104, rotate, and the feed appliance 54 that is connected on the gear unit 30 also rotates on the represented direction of arrow 104 at the gear unit 30 that has second gear 32 on its lateral wall.
In addition, the oscillating movement of piston portion 40 on arrow 102 represented directions is delivered on the gear unit 30.Therefore, the feed appliance 54 that is connected on the rotary driving source of vibration rotates on the represented direction of arrow 104, and also vibrates on the direction shown in the arrow 106 as shown in Figure 2.
As a result, feed appliance 54 vibrates in powder introducing device 57 and rotates, and can be sent to stirring and mixing arrangement 110 to powder effectively.
The rotary driving source of another kind of vibration is described below with reference to Fig. 4.As shown in FIG. 4, the rotary driving source of this vibration has first turning cylinder 91 that is connected on first motor 90; Be connected to the eccentric cam 93 on first turning cylinder 91, prejudicially and the axle 94 of rotatably mounted eccentric cam 93; Be connected to the axis of oscillation 95 on the axle 94; Put the box 96 of motor, this box is connected on the axis of oscillation 95 at the one end, and the base plate 97 of the other end is fixed on second motor 98; Be passed in the through hole that forms in the base plate 97 of the box 96 of putting motor and be rotatably connected to second turning cylinder 99 on second motor 98; And the coupling part 101 that second turning cylinder 99 and feed appliance 54 are coupled together.
To be described in the operation of the rotary driving source of the vibration shown in Fig. 4 now.
When driving first motor 90,92 rotations of first turning cylinder, the rotation of first turning cylinder 91 is delivered on the eccentric cam 93, and the rotation of eccentric cam 93 makes the axis of oscillation 95 that is connected on the axle 94 move with mode of oscillation, and makes box 96 vibrations of putting motor.At this moment, drive second motor 98 on the base plate 97 be fixed to the box 96 of putting motor, be connected to second turning cylinder, 99 rotations on second motor 98 so that pass the through hole of base plate 97.Therefore, drive first motor 90 and second motor 98 simultaneously, move with mode of oscillation so that put the box 96 of motor, and, be rotatably connected to second turning cylinder, 99 rotations on the box 96 of putting motor.Like this, the feed appliance 54 that is connected on second turning cylinder 99 by coupling part 101 rotates with mode of oscillation.
The rotary driving source of another kind of vibration is described with reference to Fig. 5.As shown in FIG. 5, the rotary driving source of this vibration has a turning cylinder 104 that is fitted on the motor 102; A box 106 of putting motor, this box is connected on the turning cylinder 104 at the one end, and it has the ultrasonator 108 on the base plate 107 that is fixed to the other end; The axis of oscillation 109 that base plate 107 with the box 106 of putting motor couples together, and the coupling part 111 that axis of oscillation 109 and shaft portion 14 and/or feed appliance 54 are coupled together.Here, ultrasonator 108 can be a piezoelectric elements.
To be described in the operation of the rotary driving source of the vibration shown in Fig. 5 now.
CD-ROM drive motor 102, so that turning cylinder 104 rotations, and the rotation of turning cylinder 104 makes the box 106 of putting motor rotate.At this moment, make ultrasonator 108 vibrations on the base plate 107 that is fixed to the box 106 of putting motor, and make axis of oscillation 109 vibrations on the base plate 107 that is connected to the box 106 of putting motor.Therefore, CD-ROM drive motor 102 and ultrasonator 108 make the box 106 of putting motor rotate simultaneously, and, make axis of oscillation 109 vibrations that are connected on the box 106 of putting motor.Like this, the feed appliance 54 that is connected on the axis of oscillation 109 by coupling part 111 rotates with mode of oscillation.
Adopt the rotary driving source 53 of the vibration that is configured to as described above powder can be transported to inlet tube 55 by powder introducing device 57, and can not interrupt flowing of powder basically.Even contact with each other and bond on the feed appliance 54 near the powder of introducing the intake of powder introducing device 57 and liquid, the rotary driving source 53 by vibration can be so that the material that bonds on the feed appliance separates with feed appliance 54.Therefore, can prevent after stirring and secondary to take place when mixing assemble, and can successfully stir.
Subsequently, will the stirring of this embodiment and the operation of mixing arrangement 110 be described.
Drive the rotary driving source 53 of vibration, feed appliance 54 is expressed to powder in the inlet tube 55 by powder introducing device 57.At this moment, by pump 74 and valve 72 liquid 78 being passed liquid intake 22 is incorporated in the inlet tube 55 by fluid storage jar 76.
, powder is contacted here with liquid, forming the mixture of aggregation, and mixture is introduced in the extruded tube 60.CD-ROM drive motor 63 makes rotor 61 rotation in the extruded tube 60, with towards housing 12 extruding mixtures.
The mixture that is extruded is introduced among the upstream stirring chamber 200a of housing 12, stir and mix, stirring and married operation by the agitator 15 that driven by drive source 20 is transported to stirring chamber 200b to these mixtures continuously simultaneously, 200c, and make these mixtures change over uniform fluid by aggregation.
In addition, filter 70 will be by the stirring chamber 200a of stirring and mixing arrangement 110,200b, the filtration of material that is stirred that 200c carries continuously, and the material that will cross filtration is stored in the treatment chamber 82, and at any time or continuously with manual control or automatically operated valve door 66 by closed condition to open mode, the material discharge that will cross filtration by the floss hole 62 of the material handled goes out.At this moment, when the pressure gauge 80 that is arranged on untreated material discharge mouth 64 demonstrates predetermined pressure or higher pressure, manually or automatically handle valve 68 by closed condition to open mode, give off untreated material.
By the steam intake 88 of the stirring chamber 200a in housing 12 and/or the steam intake 85 of stirring chamber 200b steam is introduced, and can be heated the mixture in the introducing housing 12 by the pressure of regulating vapor volume and/or steam and/or dissolve and/or sterilize.In addition, also can regulate the viscosity or the reaction of mixture by the pressure of regulating vapor volume and/or steam.
Use a Mohno pump for above-described extruded tube 60, but this not exclusive selection.For example, also can use the centrifugal pump that can obtain, slush pump, perhaps tubing pump by market.
As another embodiment, when the steam intake 88 of the stirring chamber 200a in housing 12 is used as the liquid intake, can by this liquid intake introduce will with the solvent (for example water or alcohol) of powder, mix and stir with the mixture in being introduced into housing 12, to regulate the viscosity and the dilution rate of mixture.In addition, when steam intake 88 as the liquid intake, and introduce will be with the solvent of powdered reaction the time by this liquid intake, mixture and the solvent of introducing in the housing 12 stirred, react promoting.That crosses as described above is such, and above-described mixed solvent can be and the identical solvent of solvent by supplying at the liquid intake 22 of the inlet tube shown in Fig. 1 55, or a kind of different solvent.
In this embodiment, by the top of the housing 12 of Fig. 1 mixture is sent to the bottom, but this not exclusive.The structure of the housing of Fig. 1 can be turned upside down, to transmit mixture to top by the bottom.
According to the present invention, insert the liquid into mouth be arranged near the powder intake below, make and the powder of introducing can be scattered downwards, and feed appliance is rotated with mode of oscillation, so that powder is introduced in the inlet tube.Therefore, the liquid of introducing contacts with near the powder that exists the powder intake of inlet tube, even and because the deposit that the secondary gathering of powder and liquid is produced adheres on the feed appliance, also these deposits can be removed by feed appliance.In addition, feed appliance is rotated with mode of oscillation, by the powder intake secondary aggregation is introduced in the inlet tube at any time or continuously.Therefore, the agglomerate that can prevent the secondary aggregation is along with the time increases its size, and can prevent that the powder intake from being stopped up by very large secondary aggregation.
When can cause secondary to assemble because of mixing, the viscosity of the material that is stirred is very high, when perhaps similar reason needs evenly and successfully stir and mixes, can adopt stirring of the present invention and mixing arrangement.
Claims (24)
1. a stirring and mixing arrangement with inlet tube, it comprises the powder intake, at least one is arranged near the following liquid intake of described powder intake, carry the feed appliance of powder and powder and mixtures of liquids, and make the rotary driving source of described feed appliance with the vibration of mode of oscillation rotation.
2. according to described stirring of claim 1 and mixing arrangement, it is characterized in that,
At least be provided with the helical blade of carrying powder in the position of described liquid intake or at the position of described liquid intake the following stated feed appliance, and
The size of the helical blade of described conveying powder makes its side partly reach near the madial wall of described inlet tube.
3. according to described stirring of claim 1 and mixing arrangement, it is characterized in that described feed appliance is provided with at least one cut-off blade, be used for cutting powder and mixtures of liquids.
4. according to described stirring of claim 2 and mixing arrangement, it is characterized in that described feed appliance is provided with at least one cut-off blade, be used for cutting powder and mixtures of liquids.
5. according to described stirring of claim 1 and mixing arrangement, it is characterized in that it also comprises:
Overfall, it be arranged on described powder intake below, and above described liquid intake.
6. according to described stirring of claim 2 and mixing arrangement, it is characterized in that it also comprises:
Overfall, it be arranged on described powder intake below, and above described liquid intake.
7. according to described stirring of claim 3 and mixing arrangement, it is characterized in that it also comprises:
Overfall, it be arranged on described powder intake below, and above described liquid intake.
8. according to described stirring of claim 4 and mixing arrangement, it is characterized in that it also comprises:
Overfall, it be arranged on described powder intake below, and above described liquid intake.
9. according to described stirring of claim 1 and mixing arrangement, it is characterized in that it also comprises:
Extruded tube, it is connected on the end parts of described inlet tube, and will be expressed to an end parts by powder and the mixtures of liquids that described inlet tube is introduced;
Housing, described this housing is connected on the described extruded tube, and is provided with passage, and the fluid of the feasible mixture that is extruded is by described channel flow; And
Agitator, it is arranged in the described housing, and comprises the stirring vane on shaft portion that is connected on the oscillation source and the outer surface that is attached to described shaft portion.
10. according to described stirring of claim 2 and mixing arrangement, it is characterized in that it also comprises:
Extruded tube, it is connected on the end parts of described inlet tube, and will be expressed to an end parts by powder and the mixtures of liquids that described inlet tube is introduced;
Housing, it is connected on the described extruded tube, and is provided with passage, and the fluid of the feasible mixture that is extruded is by described channel flow; And
Agitator, it is arranged in the described housing, and comprises the stirring vane on shaft portion that is connected on the oscillation source and the outer surface that is attached to described shaft portion.
11., it is characterized in that it also comprises according to described stirring of claim 3 and mixing arrangement:
Extruded tube, it is connected on the end parts of described inlet tube, and will be expressed to an end parts by powder and the mixtures of liquids that described inlet tube is introduced;
Housing, it is connected on the described extruded tube, and is provided with passage, and the fluid of the feasible mixture that is extruded is by described channel flow; And
Agitator, it is arranged in the described housing, and comprises the stirring vane on shaft portion that is connected on the oscillation source and the outer surface that is attached to described shaft portion.
12., it is characterized in that it also comprises according to described stirring of claim 4 and mixing arrangement:
Extruded tube, it is connected on the end parts of described inlet tube, and will be expressed to an end parts by powder and the mixtures of liquids that described inlet tube is introduced;
Housing, it is connected on the described extruded tube, and is provided with passage, and the fluid of the feasible mixture that is extruded is by described channel flow; And
Agitator, it is arranged in the described housing, and comprises the stirring vane on shaft portion that is connected on the oscillation source and the outer surface that is attached to described shaft portion.
13., it is characterized in that it is gone back and draws together according to described stirring of claim 5 and mixing arrangement:
Extruded tube, it is connected on the end parts of described inlet tube, and will be expressed to an end parts by powder and the mixtures of liquids that described inlet tube is introduced;
Housing, it is connected on the described extruded tube, and is provided with passage, and the fluid of the feasible mixture that is extruded is by described channel flow; And
Agitator, it is arranged in the described housing, and comprises the stirring vane on shaft portion that is connected on the oscillation source and the outer surface that is attached to described shaft portion.
14., it is characterized in that it also comprises according to described stirring of claim 6 and mixing arrangement:
Extruded tube, it is connected on the end parts of described inlet tube, and will be expressed to an end parts by powder and the mixtures of liquids that described inlet tube is introduced;
Housing, it is connected on the described extruded tube, and is provided with passage, and the fluid of the feasible mixture that is extruded is by described channel flow; And
Agitator, it is arranged in the described housing, and comprises the stirring vane on shaft portion that is connected on the oscillation source and the outer surface that is attached to described shaft portion.
15., it is characterized in that it also comprises according to described stirring of claim 7 and mixing arrangement:
Extruded tube, it is connected on the end parts of described inlet tube, and will be expressed to an end parts by powder and the mixtures of liquids that inlet tube is introduced;
Housing, it is connected on the described extruded tube, and is provided with passage, and the fluid of the feasible mixture that is extruded is by described channel flow; And
Agitator, it is arranged in the described housing, and comprises the stirring vane on shaft portion that is connected on the oscillation source and the outer surface that is attached to described shaft portion.
16., it is characterized in that it also comprises according to described stirring of claim 8 and mixing arrangement:
Extruded tube, it is connected on the end parts of described inlet tube, and will be expressed to an end parts by powder and the mixtures of liquids that described inlet tube is introduced;
Housing, it is connected on the described extruded tube, and is provided with passage, and the fluid of the feasible mixture that is extruded is by described channel flow; And
Agitator, it is arranged in the described housing, and comprises the stirring vane on shaft portion that is connected on the oscillation source and the outer surface that is attached to described shaft portion.
17. according to described stirring of claim 9 and mixing arrangement, it is characterized in that,
Described feed appliance comprises that also the first axle part divides and the second axle part branch; And
The rotary driving source of vibration comprises and is used to make the ROTATING SOURCE of described the first axle part branch rotation and is used to make described the second axle part to divide the oscillation source of vibration.
18. according to described stirring of claim 9 and mixing arrangement, it is characterized in that, by passage separately being provided with at least one stirring chamber in described housing by distribution plate.
19. according to described stirring of claim 9 and mixing arrangement, it is characterized in that,
Described housing also is provided with a floss hole; And
Be used for filter that the content in the described housing is filtered, this filter is arranged near the described floss hole.
20., it is characterized in that it also comprises according to described stirring of claim 9 and mixing arrangement:
At least one steam intake is incorporated into steam in the described housing by it.
21., it is characterized in that the pressure by regulating vapor volume and/or steam is to being introduced into mixture in the described housing and heating and/or dissolve and/or sterilizing according to described stirring of claim 9 and mixing arrangement.
22. according to described stirring of claim 9 and mixing arrangement, it is characterized in that, regulate the viscosity or the reaction of mixture by the pressure of regulating vapor volume and/or steam.
23., it is characterized in that it also comprises according to described stirring of claim 9 and mixing arrangement:
At least one liquid intake inserts the liquid in the described housing by it.
24. according to described stirring of claim 23 and mixing arrangement, it is characterized in that, regulate the viscosity or the reaction of mixture by regulating the amount of liquid of introducing.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2004354736 | 2004-12-07 | ||
| JP2004354736 | 2004-12-07 | ||
| JP2005219673 | 2005-07-28 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1803267A true CN1803267A (en) | 2006-07-19 |
Family
ID=36865491
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200510129550 Pending CN1803267A (en) | 2004-12-07 | 2005-12-06 | Stirring and mixing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1803267A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102896727A (en) * | 2012-10-19 | 2013-01-30 | 万国骅 | Combined type hybrid pouring device of foaming machine |
| CN103084082A (en) * | 2012-12-19 | 2013-05-08 | 梁锦伟 | Rapid blender |
| CN105983355A (en) * | 2015-03-20 | 2016-10-05 | 新东工业株式会社 | Heating uniformly-mixing device with steam as heating source |
| CN109012289A (en) * | 2018-09-10 | 2018-12-18 | 江苏天泽教育咨询有限公司 | A kind of water treatment agent material high pressure mixing device |
| CN109876687A (en) * | 2017-12-06 | 2019-06-14 | 天津发洋环保科技有限公司 | A kind of photo-catalytic emulsion continuous production device |
| CN110606384A (en) * | 2019-09-16 | 2019-12-24 | 安徽格闰科技控股有限公司 | Intelligent automatic feeding system |
-
2005
- 2005-12-06 CN CN 200510129550 patent/CN1803267A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102896727A (en) * | 2012-10-19 | 2013-01-30 | 万国骅 | Combined type hybrid pouring device of foaming machine |
| CN103084082A (en) * | 2012-12-19 | 2013-05-08 | 梁锦伟 | Rapid blender |
| CN105983355A (en) * | 2015-03-20 | 2016-10-05 | 新东工业株式会社 | Heating uniformly-mixing device with steam as heating source |
| CN109876687A (en) * | 2017-12-06 | 2019-06-14 | 天津发洋环保科技有限公司 | A kind of photo-catalytic emulsion continuous production device |
| CN109012289A (en) * | 2018-09-10 | 2018-12-18 | 江苏天泽教育咨询有限公司 | A kind of water treatment agent material high pressure mixing device |
| CN110606384A (en) * | 2019-09-16 | 2019-12-24 | 安徽格闰科技控股有限公司 | Intelligent automatic feeding system |
| CN110606384B (en) * | 2019-09-16 | 2021-05-11 | 安徽格闰科技控股有限公司 | Intelligent automatic feeding system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US20060120212A1 (en) | Stirring and mixing device | |
| EP1527812B1 (en) | Agitation mixer | |
| CN1803267A (en) | Stirring and mixing device | |
| CN1830570A (en) | Medium mixing up of wet-type dispersion machine | |
| JP2007105590A (en) | Stirring/mixing system, and concentration control method using the system | |
| CN117101461B (en) | Medicine mixing equipment for marine ecological management | |
| CN211586778U (en) | Grinding and stirring integrated machine for refractory slurry production | |
| CN101050863A (en) | Method and device for producing coal water fluid | |
| CN112354407A (en) | Double-hopper feeding medicament mixing device based on quantification | |
| JP2005131578A (en) | Agitation mixer | |
| CN219252498U (en) | Compound stirring mixing device of water treatment medicament | |
| CN115869794A (en) | Device and equipment for mixing and dispersing solid and liquid | |
| CN219463164U (en) | Mixing device for waterproof material production | |
| CN117959977A (en) | Functional composite fracturing fluid thickener and preparation device thereof | |
| CN111974335A (en) | Heavy metal passivator apparatus for producing | |
| CN217910205U (en) | Diamond particle stirring device | |
| WO1992021437A1 (en) | Apparatus for blending a powder with a liquid | |
| CN1541758A (en) | Fluid continuous mixing device | |
| JP2004060326A (en) | Method and device for manufacturing lightweight solidification material, pipe-shaped mixer device, solidification material manufacturing device and specific gravity adjusting device | |
| CN209828763U (en) | Kneading machine capable of increasing running speed of paddle | |
| CN213112552U (en) | Nano calcium carbonate reaction stirring device | |
| JP2006102600A (en) | Stirring/mixing apparatus | |
| CN219376858U (en) | Efficient mixing device for pesticide powder products | |
| CN220361118U (en) | Stuffing mixer with quantitative feeding mechanism | |
| CN217909835U (en) | Accelerator apparatus for producing |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Open date: 20060719 |