CN201371045Y

CN201371045Y - Three-cavity horizontal type mixing device

Info

Publication number: CN201371045Y
Application number: CN200820208494U
Authority: CN
Inventors: 刘�英
Original assignee: Shanghai Yichen Information Technology Development Co Ltd
Current assignee: Shanghai Yichen Information Technology Development Co Ltd
Priority date: 2008-12-31
Filing date: 2008-12-31
Publication date: 2009-12-30
Anticipated expiration: 2018-12-31

Abstract

The utility model relates to a three-cavity horizontal type mixing device, which is particularly suitable for the uniform mixing of solid powder, liquid, additive agent and the like with the solid-liquid mixture with high viscosity. The three-cavity horizontal type mixing device comprises a feeding system (201), an outer casing (204), a discharging system (209), a material transmitting system (200), a first cavity shell and a second cavity shell which are intersected in a hollow cylinder structure and a third cavity shell (207) arranged on the bottom of the first cavity shell and the second cavity shell. A first cavity body (205), a second cavity body (206) and a third cavity body (208) which have mutually parallel axles; a turning axle (501), a second turning axle (502) and a third turning axle (503) which are respectively positioned at the circle centers of the three cavity bodies; and a first mixing system (6), a second mixing system (7) and a third mixing system (8) which are respectively positioned on the three turning axles and rotate along with the three turning axles, are arranged in the mixing device.

Description

A kind of three-cavity horizontal mixing arrangement

Technical field

The utility model relates to a kind of horizontal type mixing device, and particularly a kind of three-cavity horizontal mixing arrangement belongs to the mechanical mixing equipment field.

Background technology

In the reconstituted rice process, liquid such as the pressed powder of cereal and water evenly need be mixed, obtain the high solidliquid mixture of viscosity, and in the above-mentioned solidliquid mixture, need further evenly to add various solids and/or liquid additive again.And above-mentioned various material need be evenly distributed in the gained solidliquid mixture, so that each content of material of the reconstituted rice that makes meets standard.

Yet because the viscosity height of the pressed powder of cereal and the solidliquid mixture that obtains after water mixes, the various liquid of further interpolation, pressed powder, additive etc. are difficult to be evenly distributed in wherein thereafter.Especially in the mixed process of the solidliquid mixture that pressed powder and viscosity are high, can produce the secondary aggregation particle of pressed powder, that is, powder ball, this powder ball outside is the mixture of powder and high viscosity solidliquid mixture, and is inner then be not have the pressed powder that mixes.Even and if in mixed process, stir, in considerable time, still can mix inhomogeneously, the secondary aggregation through producing is distributed in the mixture very difficult once more.Simultaneously, in the high solidliquid mixture of viscosity, add liquid and pressed powder if desired simultaneously, also can bring the secondary aggregation problem owing to mixing between the liquid of interpolation and the pressed powder.

If adopt the high solidliquid mixture of a spot of liquid, pressed powder, additive and viscosity to mix, though can obtain mixture comparatively uniformly, but the speed of mixing is slower, and the gained mixture is less, can't satisfy large batch of need of industrial production.

In the Chinese patent application 03164908.4 based on Japanese patent application 278598/202,21188/2003,185502/2003, a kind of mixing stirring device and stirring mixing method are disclosed, this device comprises the mixer of an approximate circle tubular, its inside has stirring vane, powder enters mixer with liquid by different inlets, under the stirring of stirring vane, mix then.Formed compartment between the stirring vane, mix thereby powder and liquid are separated into some groups, yet in actual mixed process, mix can't be good divide into groups, and can stockpile on the inwall of mixer and a large amount of mixture, can't evenly be stirred.And this device is not suitable for mixing of powder and high viscosity solidliquid mixture.

Among PCT International Application PCT/US2003/011426, a kind of mixing apparatus is disclosed, this equipment comprises that a bottom is full of the bucket of liquid, one is inserted in the liquid and inner vertical conduit with rotating vane, pressed powder has the part of liquid from the conduit of this vertical conduit interpolation from top to bottom, and under the effect of stirring vane and liquid mix, and then a bucket neutralising fluid that is distributed to the conduit outside further mixes.Yet this equipment is applicable to a spot of pressed powder is distributed in a large amount of liquid, and the gained solidliquid mixture can not have viscosity higher, otherwise will stop up conduit.

In the Chinese patent application 03122966.2 based on Japan Patent, the mixing arrangement and the method thereof of a kind of powder and liquid are disclosed, powder is dispersed from the top of mixer and is fallen in this device, and the liquid that sprays all around with container in dropping process mixes mutually then.Though this mixed method can allow powder and liquid disperse to mix to a certain extent, avoid powder ball to produce, the powder of not all whereabouts can mix with the liquid that sprays then, and unmixing powder and liquid are fallen the bottom of mixer, still can not evenly mix.Simultaneously, having full-bodied solidliquid mixture can't spray around the container, so this device is not suitable for mixing of powder and high viscosity solidliquid mixture.

In the Chinese patent application 200410084721.1, a kind of vertical solid-liquid mixing arrangement and mixed method are disclosed, this device comprises one group of baffle plate that is provided with along the mixer inwall, mixer is divided into the teeter chamber of some hollows, and the powder and the liquid that utilize one group of stirring vane of mixer central authorities to stir in each teeter chamber then mix.Yet because the existence of the teeter chamber of horizontal hollow, each material that feeds intake from the mixer top will be saved bit by bit in a large number in several teeter chambers on top, and the inequality that causes material in each teeter chamber to distribute, if powder and mixtures of liquids have viscosity higher simultaneously, this mixture also will block mixer because of the existence of each baffle plate and teeter chamber.Simultaneously single powder adds inlet, can cause material can not evenly distribute along all directions on the cross section of mixer.

Simultaneously Chinese patent 200610011506.8 and European patent EP 06113920.0 disclose two kinds of static mixing devices respectively, utilize the shunting of each material, mix, yet said apparatus are not suitable for mixing of powder and high viscosity solidliquid mixture.

Simultaneously in the Chinese patent 200410090534.4, disclose the horizontal type mixing device that a kind of inside has stirring vane, powder and liquid from the top and bottom injection device of a side of horizontal type mixing device, utilize blade to mix respectively then.Need in having full-bodied solidliquid mixture, to add simultaneously liquid and pressed powder yet this device can't solve, and avoid producing between the liquid that adds and the pressed powder problem of powder ball simultaneously.

Except above-mentioned points, Chinese patent 200510009386.3,200510042674.9,200510129550.4,200510103613.9 etc. also all discloses multiple mixing arrangement, yet said apparatus is still failed to solve the high solidliquid mixture of viscosity and liquid, pressed powder, additive etc. and carried out mixed uniformly technical problem according to a certain ratio.

Summary of the invention

A purpose of the present utility model is to provide a kind of three-cavity horizontal mixing arrangement, solidliquid mixture and pressed powder, liquid, additive etc. evenly can be mixed according to a certain ratio by this device, be specially adapted to the even mixing of high solidliquid mixture of viscosity and pressed powder, liquid, additive.

A kind of three-cavity horizontal mixing arrangement disclosed in the utility model comprises feed system 201, the first chamber shell 202, the second chamber shell 203, the 3rd chamber shell 207, outer casing 204, first rotating shaft 501, second rotating shaft 502, the 3rd rotating shaft 503, first stirring system 6, second stirring system 7, the 3rd stirring system 8, material transfer system 200 and discharge system 209.

The described first chamber shell 202 and the second chamber shell 203 are two hollow cylinder structures that intersect, described the 3rd chamber shell 207 is positioned at the bottom of the first chamber shell 202, the second chamber shell 203, and interconnect by material transfer system 200 and both, the axle center of three cavitys is parallel to each other, and is positioned at the inside of outer casing 204.

The described first chamber shell 202 inside are formed with first cavity, 205, the second chamber shells, 203 inside and are formed with second cavity, 206, the three chamber shells, 207 inside and are formed with the 3rd cavity 208, and described first cavity 205, second cavity 206 and the 3rd cavity 208 are interconnected.

Described first rotating shaft 501 is positioned at first cavity, 205 inside, and by its center of circle.Described first stirring system 6 is connected in first rotating shaft 501, and rotates thereupon.

Described first stirring system 6 is one group of impeller that are connected in first rotating shaft 501, and described each impeller comprises 2～4 blades that include agitating plate 602 and material scraping plate 603, and interlobate angular interval equates.One end of described agitating plate 602 is connected in the rotating shaft 501, and the other end is connected with material scraping plate 603, and the inwall of this material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 2mm～20mm.

Described agitating plate 602 is a sector structure, and its center of circle angle is 10 °～45 °, and its internal diameter equates that with rotating shaft 501 external diameters its external diameter is the poor of the first chamber shell, 202 internal diameters and material scraping plate 603 thickness.

Described material scraping plate 603 is a sector structure, and its center of circle angle equates that with the center of circle angle of its agitating plate that is connected 602 its internal diameter equates that with agitating plate 602 external diameters its external diameter equates with the first chamber shell, 202 internal diameters.

Described material scraping plate 603 is in same plane, 603 one-tenth 0 °～45 ° angles of described agitating plate 602 and perpendicular and material scraping plate, preferred 30 ° of angles with perpendicular.

The agitating plate of each impeller of described first stirring system 6 is adjacent staggered 0 °～45 ° angles between the agitating plate of impeller.

The interval of respectively organizing between the impeller of described first stirring system 6 equates.

Described second rotating shaft 502 is positioned at second cavity, 206 inside, and by its center of circle.Described second stirring system 7 is connected in second rotating shaft 502, and rotates thereupon.

Described second stirring system 7 is one group of impeller that are connected in second rotating shaft 502, and described each impeller comprises 2～4 blades that include agitating plate 702 and material scraping plate 703, and interlobate angular interval equates.One end of described agitating plate 702 is connected in the rotating shaft 502, and the other end is connected with material scraping plate 703, and the inwall of this material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 2mm～20mm.

Described agitating plate 702 is a sector structure, and its center of circle angle is 10 °～45 °, and its internal diameter equates that with rotating shaft 502 external diameters its external diameter is the poor of the second chamber shell, 203 internal diameters and material scraping plate 703 thickness.

Described material scraping plate 703 is a sector structure, and its center of circle angle equates that with the center of circle angle of its agitating plate that is connected 702 its internal diameter equates that with agitating plate 702 external diameters its external diameter equates with the second chamber shell, 203 internal diameters.

Described material scraping plate 703 is in same plane, 703 one-tenth 0 °～45 ° angles of described agitating plate 702 and perpendicular and material scraping plate, preferred 30 ° of angles with perpendicular.

The agitating plate of each impeller of described second stirring system 7 is adjacent staggered 0 °～45 ° angles between the agitating plate of impeller.

The interval of respectively organizing between the impeller of described second stirring system 7 equates.

Described the 3rd rotating shaft 503 is positioned at the 3rd cavity 208 inside, and by its center of circle.Described the 3rd stirring system 8 is connected in the 3rd rotating shaft 503, and rotates thereupon.

Described the 3rd stirring system 8 is one group of impeller that are connected in the 3rd rotating shaft 503, and described each impeller comprises 2～4 blades that include agitating plate 802 and material scraping plate 803, and interlobate angular interval equates.One end of described stirring piece 802 is connected in the rotating shaft 503, and the other end is connected with material scraping plate 803, and the inwall of this material scraping plate 803 and the 3rd chamber shell 207 is tangent, and leaves the safety clearance of 2mm～20mm.

Described stirring piece 802 is a sector structure, and its center of circle angle is 10 °～45 °, and its internal diameter equates that with rotating shaft 503 external diameters its external diameter is the poor of the 3rd chamber shell 207 internal diameters and material scraping plate 803 thickness.

Described material scraping plate 803 is a sector structure, and its center of circle angle equates that with the center of circle angle of its stirring piece that is connected 802 its internal diameter equates that with stirring piece 802 external diameters its external diameter equates with the 3rd chamber shell 207 internal diameters.

Described material scraping plate 803 is in same plane, 803 one-tenth 20 °～65 ° angles of described stirring piece 802 and perpendicular and material scraping plate, preferred 45 ° of angles with perpendicular.

The stirring piece of each impeller of described the 3rd stirring system 8 is adjacent staggered 0 °～45 ° angles between the stirring piece of impeller.

The interval of respectively organizing between the impeller of described the 3rd stirring system 8 equates.

The impeller of the impeller of described first stirring system 6 and second stirring system 7 is staggered, be distributed with the impeller of one group of second stirring system 7 between the impeller of wantonly two groups of first adjacent stirring systems 6, and these first stirring system, 6 impellers equate with the spacing of these second stirring system, 7 impellers with spacing and another first stirring system, 6 impellers of second stirring system, 7 impellers.Material scraping plate on arbitrary blade of arbitrary impeller of described second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 2mm～20mm.

The radius of the described first chamber shell 202 and the second chamber shell 203 equates.The diameter of described the 3rd chamber shell 207 is the first chamber shell, 202 radiuses, first rotating shaft, 501 radiuses and the second chamber shell, 203 diameter sums.Described first rotating shaft 501 and second rotating shaft 502 are done and are relatively rotated.The rotating ratio of described first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 2.2: 2.2: 1～4.6: 4.6: 1.

The described outer casing 204 and the first chamber shell 202 further comprise the position thereon and pass wherein the first chamber door 2020, so that when opening the described first chamber door 2020, expose first cavity 205.The described outer casing 204 and the second chamber shell 203 further comprise the position thereon and pass wherein the second chamber door 2030, so that when opening the described second chamber door 2030, expose second cavity 206.Described outer casing 204 and the 3rd chamber shell 207 further comprise the position thereon and pass wherein the 3rd chamber door 2070, so that when opening described the 3rd chamber door 2070, expose the 3rd cavity 208.

Described feed system 201 comprises feeding-in solid body mouth 2011, liquid inlet opening 2012, the first additive charging aperture 2013, the second additive charging aperture 2014.Described feeding-in solid body mouth 2011 and liquid inlet opening 2012 are adjacent to be arranged on described outer casing 204 end faces, and penetrate described outer casing 204 and the first chamber shell 202, the second chamber shell 203 respectively, are communicated with described first cavity 205 and second cavity 206.The described first additive charging aperture 2013, the second additive charging aperture 2014 are arranged on described outer casing 204 end faces, and penetrate the described outer casing 204 and the first chamber shell 202, are communicated with described first cavity 205.Described material transfer system 200 is arranged on the outer casing 204, and penetrates outer casing 204, the first chamber shell 202, the second chamber shell 203 and the 3rd chamber shell 207, is communicated with first cavity 205, second cavity 206 and the 3rd cavity 208.Described discharge system 209 is arranged on described outer casing 204 bottom surfaces, and penetrates described outer casing 204 and the 3rd chamber shell 207, is communicated with described the 3rd cavity 208.

The process that adopts the three-cavity horizontal mixing arrangement to mix comprises following steps:

Step 1: enter first cavity 205 and second cavity 206 from the premix material inlet input premix material of outer casing 204 bottoms, and under the rotation stirring action of first stirring system 6 and second stirring system 7, be evenly distributed on first cavity 205 and the 2 206 inside.

Step 2: enter first cavity, 205 inside from described feeding-in solid body mouth 2011 input pressed powders, under the rotation stirring action of first stirring system 6, described pressed powder mixes with the premix material is full and uniform.

Step 3: simultaneously, enter second cavity, 206 inside from described liquid inlet opening 2012 input gases, liquid or gas-liquid mixture, under the rotation stirring action of second stirring system 7, described gas, liquid or gas-liquid mixture mix with the premix material is full and uniform.

Step 4: under the relative rotation stirring action of first stirring system 6 and second stirring system 7, be mixed with the premix material and the full and uniform mixing of premix material that is mixed with gas, liquid or gas-liquid mixture of pressed powder, obtain mixed material.

Described mixed material is under the effect of the agitating plate 602 of each impeller of first stirring system 6 and second stirring system 7 and 702, to first cavity 206 and the transmission of second cavity, 207 rear portions.

The

material scraping plate

603 and 703 of each impeller of first stirring system 6 and second stirring system 7 strikes off the material that adheres on the first chamber shell, 202 inwalls, the second chamber shell, 203 inwalls respectively, to mix once more.

Step 5: enter first cavity 206 and second cavity 207 from the first additive charging aperture, 2013 input additives, under the rotation stirring action of first stirring system 6 and second stirring system 7, the full and uniform mixing of described additive and mixed material obtains containing the mixed material of additive.

The described mixed material that contains additive is under the effect of the agitating plate 602 of each impeller of first stirring system 6 and second stirring system 7 and 702, to first cavity 206 and the transmission of second cavity, 207 rear portions.

The

material scraping plate

Step 6: enter first cavity 206 and second cavity 207 from the second additive charging aperture, 2014 input additives, under the rotation stirring action of first stirring system 6 and second stirring system 7, the full and uniform mixing of described additive and mixed material obtains mixture.

Described mixture is under the effect of the agitating plate 602 of each impeller of first stirring system 6 and second stirring system 7 and 702, to first cavity 206 and the transmission of second cavity, 207 rear portions.

The

material scraping plate

Step 7: by the agitating plate 602 of each impeller of first stirring system 6 and second stirring system 7 and 702 rotation stirring and gravity effect, described mixture transfers to the 3rd cavity 208 by material transfer system 200.

Step 8: enter the 3rd cavity 208 from material transfer system 200 input mixtures, under the rotation stirring action of the 3rd stirring system 8, described mixture carries out further evenly mixing, and obtains well-mixed mixture.

Described well-mixed mixture transmits to the 3rd cavity 208 rear portions under the effect of the agitating plate 802 of the 3rd stirring system 8 each impeller.

The material scraping plate 803 of the 3rd stirring system 8 each impeller strikes off the material that adheres on the 3rd chamber shell 207 inwalls, to mix once more.

Step 9: by the rotation stirring and the gravity effect of the agitating plate 802 of the 3rd stirring system 8 each impeller, described mixture is by discharge system 209 outputs.

Utilize said apparatus and method, the premix material inlet input premix material from outer casing 204 bottoms under the stirring of first stirring system 6 and second stirring system 7, is evenly distributed on first cavity 205 and second cavity, 206 inside.Add pressed powders and liquid enters first cavity 205 and second cavity 206 from feeding-in solid body mouth 2011 and liquid inlet opening 2012 this moment simultaneously, pressed powder evenly mixes in first cavity, 205 inside and premix material, inner and premix material evenly mixes liquid at second cavity 206, thereby has avoided the secondary aggregation that brings owing to mixing between the pressed powder that adds and the liquid.First stirring system 6 and second stirring system 7 in relative rotation afterwards, the premix material that is added with the premix material of pressed powder and be added with liquid is carried out once more mixing, the mixing of this moment is equivalent to the solidliquid mixture that viscosity, density is high slightly and viscosity, solidliquid mixture of the same race that density is low slightly mixes, and the mixing of this moment is very easy to carry out and mix easily.Import additive by the first additive charging aperture 2013 and the second additive charging aperture 2014 to mixture subsequently, this moment is owing to exist two cavitys, the additive of input is dispersed into two groups under the drive of stirring system, every group of internal additives disperses to mix, under the drive of stirring system, disperse once more between two groups then to mix, setting by two cavitys and two stirring systems, once Shu Ru material can carry out repeatedly dispersion and mixing, thereby reach the purpose of full and uniform mixing and avoid the secondary aggregation phenomenon, be i.e. the powder ball phenomenon.To sum up, essence of the present utility model is the existence by two cavitys and two stirring systems, make the material quilt frequently of inside cavity respectively organize impeller and be divided into two groups at random, every group is mixed voluntarily, two groups are driven mutually the impeller that changes once more and are mixed then, this repeatedly random packet and again mixing make each composition of material inside by repeatedly random packet and mix the equally distributed state that reaches at random.

Simultaneously respectively organizing of stirring system staggeredly between the impeller has certain angle, is convenient to the described random packet and the carrying out of mixing at random more.Simultaneously agitating plate and the vertical plane of each impeller blade have a certain degree, and are convenient to the high mixture of viscosity and transmit to the other end from an end of mixing arrangement inside.

By said apparatus and method, the utility model utilization random packet and mixing has at random repeatedly effectively been avoided the variety of issue that exists in the mixed process of high viscosity solidliquid mixture and pressed powder, liquid, additive etc., can be fast, lasting, stable high viscosity solidliquid mixture, pressed powder, liquid, additive being mixed uniformly with certain proportioning.

Description of drawings

Fig. 1 is the overall structure side view of three-cavity horizontal mixing arrangement of the present utility model.

Fig. 2 is the viewgraph of cross-section of three-cavity horizontal mixing arrangement of the present utility model along the A-A ' of Fig. 1.

Fig. 3 is the viewgraph of cross-section of three-cavity horizontal mixing arrangement of the present utility model along the B-B ' of Fig. 1.

Fig. 4 is the viewgraph of cross-section of three-cavity horizontal mixing arrangement of the present utility model along the C-C ' of Fig. 1.

Fig. 5 is the viewgraph of cross-section of three-cavity horizontal mixing arrangement of the present utility model along the D-D ' of Fig. 1.

Fig. 6 is the viewgraph of cross-section of three-cavity horizontal mixing arrangement of the present utility model along the E-E ' of Fig. 1.

Fig. 7 is the agitating plate of three-cavity horizontal mixing arrangement of the present utility model and the side view of material scraping plate.

Fig. 8 a, 8b, 8c, 8d are the schematic diagrames of stagger angle relation between each impeller of one group of adjacent impeller of three-cavity horizontal mixing arrangement of the present utility model.

The specific embodiment

According to claim of the present utility model and the disclosed content of utility model content, the technical solution of the utility model is specific as follows described.

Embodiment one:

A kind of three-cavity horizontal mixing arrangement comprises as the lower part:

According to Fig. 1, Fig. 2 and Fig. 4:

A kind of three-cavity horizontal mixing arrangement comprises feed system 201, the first chamber shell 202, the second chamber shell 203, the 3rd chamber shell 207, outer casing 204, first rotating shaft 501, second rotating shaft 502, the 3rd rotating shaft 503, first stirring system 6, second stirring system 7, the 3rd stirring system 8, material transfer system 200 and discharge system 209.

According to Fig. 2 and Fig. 4:

Described first stirring system 6 is one group of impeller that are connected in first rotating shaft 501, and described each impeller comprises 2～4 blades that include agitating plate 602 and material scraping plate 603, and interlobate angular interval e equates.One end of described agitating plate 602 is connected in the rotating shaft 501, and the other end is connected with material scraping plate 603, and the inwall of this material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 2mm～20mm.

Described agitating plate 602 is a sector structure, and its central angle d is 10 °～45 °, and its internal diameter equates that with rotating shaft 501 external diameters its external diameter is the poor of the first chamber shell, 202 internal diameters and material scraping plate 603 thickness.

According to Fig. 2 and Fig. 4:

Described second stirring system 7 is one group of impeller that are connected in second rotating shaft 502, and described each impeller comprises 2～4 blades that include agitating plate 702 and material scraping plate 703, and interlobate angular interval e ' equates.One end of described agitating plate 702 is connected in the rotating shaft 502, and the other end is connected with material scraping plate 703, and the inwall of this material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 2mm～20mm.

Described agitating plate 702 is a sector structure, and its central angle d ' is 10 °～45 °, and its internal diameter equates that with rotating shaft 502 external diameters its external diameter is the poor of the second chamber shell, 203 internal diameters and material scraping plate 703 thickness.

According to Fig. 3 and Fig. 4:

Described the 3rd stirring system 8 is one group of impeller that are connected in the 3rd rotating shaft 503, and described each impeller comprises 2～4 blades that include agitating plate 802 and material scraping plate 803, interlobate angular interval e " equate.One end of described stirring piece 802 is connected in the rotating shaft 503, and the other end is connected with material scraping plate 803, and the inwall of this material scraping plate 803 and the 3rd chamber shell 207 is tangent, and leaves the safety clearance of 2mm～20mm.

Described stirring piece 802 is a sector structure, its central angle d " be 10 °～45 °, its internal diameter equates that with rotating shaft 503 external diameters its external diameter is the poor of the 3rd chamber shell 207 internal diameters and material scraping plate 803 thickness.

According to Fig. 2, Fig. 3 and Fig. 8 a, 8b, 8c, 8d:

The agitating plate of each impeller of described first stirring system 6 is adjacent that staggered angle f is 0 °～45 ° between the agitating plate of impeller.

The agitating plate of each impeller of described second stirring system 7 is adjacent that staggered angle f ' is 0 °～45 ° between the agitating plate of impeller.

The stirring piece of each impeller of described the 3rd stirring system 8 is adjacent staggered angle f between the stirring piece of impeller " be 0 °～45 °.

According to Fig. 7:

Described material scraping plate 603 is in same plane with perpendicular and extends along the first chamber shell, 202 inwalls, and the angle g that described agitating plate 602 and perpendicular and material scraping plate are 603 is 0 °～45 °.

Described material scraping plate 703 is in same plane with perpendicular and extends along the second chamber shell, 203 inwalls, and the angle g ' that described agitating plate 702 and perpendicular and material scraping plate are 703 is 0 °～45 °.

Described material scraping plate 803 is in same plane with perpendicular, the angle g of described stirring piece 802 and perpendicular and material scraping plate 803 " be 20 °～65 °.

According to Fig. 4, Fig. 5 and Fig. 6:

Described first cavity 205 and second cavity 206 are divided into a plurality of chambers, and the sidewall of each chamber is respectively equipped with the first chamber door 2020 and the second chamber door 2030.

The interval of respectively organizing between the impeller of described first stirring system 6 equates, equates as the interval between impeller 60011, impeller 60012 and the impeller 60013.

The interval of respectively organizing between the impeller of described second stirring system 7 equates, equates as the interval between impeller 70011 and the impeller 70012.

The interval of respectively organizing between the impeller of described the 3rd stirring system 8 equates, equates as the interval between impeller 80011 and the impeller 80012.

The impeller of the impeller of described first stirring system 6 and second stirring system 7 is staggered.Be distributed with the impeller of one group of second stirring system 7 between the impeller of wantonly two groups of first adjacent stirring systems 6, and these first stirring system, 6 impellers equate with the spacing of these second stirring system, 7 impellers with spacing and another first stirring system, 6 impellers of second stirring system, 7 impellers.As being distributed with impeller 70011 between adjacent impeller 60011 and the impeller 60012, and the spacing between impeller 60011 and the impeller 70011 equates with spacing between impeller 70011 and the impeller 60012, be distributed with impeller 60012 between adjacent 70011 and the impeller 70012 of impeller, and the spacing between impeller 70011 and the impeller 60012 equates with spacing between impeller 60012 and the impeller 70012.

Material scraping plate on arbitrary blade of arbitrary impeller of described second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 2mm～20mm.

According to Fig. 1, Fig. 2 and Fig. 4:

The described outer casing 204 and the first chamber shell 202 further comprise the position thereon and pass wherein the first chamber door 2020, so that when opening the described first chamber door 2020, expose first cavity 205.The described outer casing 204 and the second chamber shell 203 further comprise the position thereon and pass wherein the second chamber door 2030, so that when opening the described second chamber door 2030, expose second cavity 206.

According to Fig. 1 to Fig. 6:

Described feed system 201 comprises feeding-in solid body mouth 2011, liquid inlet opening 2012, the first additive charging aperture 2013, the second additive charging aperture 2014.

Described feeding-in solid body mouth 2011 and liquid inlet opening 2012 are adjacent to be arranged on described outer casing 204 end faces, and penetrate described outer casing 204 and the first chamber shell 202, the second chamber shell 203 respectively, are communicated with described first cavity 205 and second cavity 206.

The described first additive charging aperture 2013, the second additive charging aperture 2014 are arranged on described outer casing 204 end faces, and penetrate the described outer casing 204 and the first chamber shell 202, are communicated with described first cavity 205.

Described material transfer system 200 is arranged on the outer casing 204, and penetrates outer casing 204, the first chamber shell 202, the second chamber shell 203 and the 3rd chamber shell 207, is communicated with first cavity 205, second cavity 206 and the 3rd cavity 208.

Described discharge system 209 is arranged on described outer casing 204 bottom surfaces, and penetrates described outer casing 204 and the 3rd chamber shell 207, is communicated with described the 3rd cavity 208.

According to Fig. 4:

The radius of the described first chamber shell 202 and the second chamber shell 203 equates.The diameter of described the 3rd chamber shell 207 is the first chamber shell, 202 radiuses, first rotating shaft, 501 radiuses and the second chamber shell, 203 diameter sums.

Described first rotating shaft 501 and second rotating shaft 502 are done and are relatively rotated.The rotating ratio of described first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 2.2: 2.2: 1～4.6: 4.6: 1.

According to Fig. 1 and Fig. 2:

Step 1: enter first cavity 205 and second cavity 206 from the premix material inlet input premix material of outer casing 204 bottoms, and under the rotation stirring action of first stirring system 6 and second stirring system 7, be evenly distributed on first cavity 205 and second cavity, 206 inside.

According to Fig. 2 and Fig. 5:

The

material scraping plate

According to Fig. 1 and Fig. 2

The

material scraping plate

The

material scraping plate

According to Fig. 1, Fig. 4 and Fig. 5:

According to Fig. 1, Fig. 3, Fig. 4 and Fig. 6:

According to Fig. 5, it is to be noted that above-mentioned material interpolation, dispersion and mixed process specifically carries out as follows:

In first cavity 205 and second cavity 206, be filled with solidliquid mixture.In first group of chamber of first cavity 205 and second cavity 206, from feeding-in solid body mouth 2011 input pressed powders, pressed powder fully disperses to mix with solidliquid mixture under the rotation stirring action of first group of impeller 6001 of first stirring system 6.Simultaneously, from liquid inlet opening 2012 input liquid, liquid fully disperses to mix with solidliquid mixture under the rotation stirring action of first group of impeller 7001 of second stirring system 7.The transmission backward under impeller 60011 effects of first solidliquid mixture, second batch of solidliquid mixture transmission backward under impeller 70011 effects, then because impeller 60011 and 70011 pairs of commentaries on classics of impeller, first solidliquid mixture that is mixed with pressed powder carries out the first time with the second batch of solidliquid mixture that is mixed with liquid to be mixed mutually, pressed powder that adds and liquid mix mutually and are distributed in the solidliquid mixture, above-mentioned then solidliquid mixture is divided into two batches again at random, and stirred by impeller 60012 and impeller 70012 respectively, the content that adds the pressed powder that advances in first solidliquid mixture that is stirred by impeller 60012 reduces and the content that adds the liquid that advances increases, the content that adds the pressed powder that advances in the second batch of solidliquid mixture that is stirred by impeller 70012 increases and the content that adds the liquid that advances reduces, then impeller 60012 and impeller 70012 to transfer to under, two batches of solidliquid mixtures are mixed again, pressed powder that make to add and liquid is along with secondary mutual mixing is carried out in the mixing of solidliquid mixture, and then is divided into two batches at random.Mixing at random by above-mentioned several times and separating at random, the pressed powder and the liquid of interpolation are evenly distributed in the solidliquid mixture, and also full and uniform mixing between pressed powder and the liquid.

Above-mentioned subsequently solidliquid mixture is transported to second group of chamber by first group of

impeller

6001 and 7001 back kicks, since then, from the first additive charging aperture, 2013 input additives, the solidliquid mixture that is mixed with additive is under second group of

impeller

6002 and 7002 effects, described in the past mode is carried out mixing at random repeatedly and is separated at random, so that additive evenly distributes.The gained solidliquid mixture is transported to the 3rd chamber by second impeller sets 6002 and 7002 back kicks subsequently, to mix mutually with the additive of importing from the second additive charging aperture 2014.The solidliquid mixture that mixes gained continues in some chambers subsequently, under the effect of stirring system 6 and 7, carry out mixing at random repeatedly and separate and stirring evenly distributions such as the solid-liquid powder that feasible interpolation is advanced, liquid, additive at random, obtain mixture, and output.

The 3rd cavity 208 mainly plays storing mixture, and slowly stirs, and increases the mixture holdup time so that the possible various reactions of mixture inside have time enough carry out, as crosslinked, emulsification or the like reaction.

Embodiment two:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 3mm.

Its central angle d of agitating plate 602 is 14 °.

The agitating plate of each impeller is adjacent that staggered angle f is 7 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 4 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 3mm.

The central angle d ' of agitating plate 702 is 14 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 7 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 4 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 3mm.

The central angle d of agitating plate 802 " be 14 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 7 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 24 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 3mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 2.4: 2.4: 1.

Embodiment three:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 5mm.

Its central angle d of agitating plate 602 is 17 °.

The agitating plate of each impeller is adjacent that staggered angle f is 8 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 8 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 5mm.

The central angle d ' of agitating plate 702 is 17 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 8 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 8 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 5mm.

The central angle d of agitating plate 802 " be 17 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 8 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 28 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 5mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 2.6: 2.6: 1.

Embodiment four:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 7mm.

Its central angle d of agitating plate 602 is 20 °.

The agitating plate of each impeller is adjacent that staggered angle f is 10 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 12 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 7mm.

The central angle d ' of agitating plate 702 is 20 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 10 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 12 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 7mm.

The central angle d of agitating plate 802 " be 20 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 10 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 32 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 7mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 2.8: 2.8: 1.

Embodiment five:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 9mm.

Its central angle d of agitating plate 602 is 23 °.

The agitating plate of each impeller is adjacent that staggered angle f is 11 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 16 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 9mm.

The central angle d ' of agitating plate 702 is 23 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 11 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 16 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 9mm.

The central angle d of agitating plate 802 " be 23 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 11 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 36 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 9mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 3.0: 3.0: 1.

Embodiment six:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 11mm.

Its central angle d of agitating plate 602 is 26 °.

The agitating plate of each impeller is adjacent that staggered angle f is 13 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 20 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 11mm.

The central angle d ' of agitating plate 702 is 26 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 13 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 20 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 11mm.

The central angle d of agitating plate 802 " be 26 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 13 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 40 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 11mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 3.2: 3.2: 1.

Embodiment seven:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 12mm.

Its central angle d of agitating plate 602 is 29 °.

The agitating plate of each impeller is adjacent that staggered angle f is 14 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 24 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 12mm.

The central angle d ' of agitating plate 702 is 29 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 14 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 24 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 12mm.

The central angle d of agitating plate 802 " be 29 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 14 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 44 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 12mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 3.4: 3.4: 1.

Embodiment eight:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 13mm.

Its central angle d of agitating plate 602 is 32 °.

The agitating plate of each impeller is adjacent that staggered angle f is 16 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 28 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 13mm.

The central angle d ' of agitating plate 702 is 32 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 16 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 28 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 13mm.

The central angle d of agitating plate 802 " be 32 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 16 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 48 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 13mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 3.6: 3.6: 1.

Embodiment nine:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 15mm.

Its central angle d of agitating plate 602 is 35 °.

The agitating plate of each impeller is adjacent that staggered angle f is 17 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 32 °

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 15mm.

The central angle d ' of agitating plate 702 is 35 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 17 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 32 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 15mm.

The central angle d of agitating plate 802 " be 35 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 17 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 52 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 15mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 3.8: 3.8: 1.

Embodiment ten:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 17mm.

Its central angle d of agitating plate 602 is 38 °.

The agitating plate of each impeller is adjacent that staggered angle f is 19 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 36 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 17mm.

The central angle d ' of agitating plate 702 is 38 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 19 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 36 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 17mm.

The central angle d of agitating plate 802 " be 38 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 19 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 56 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 17mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 4.0: 4.0: 1.

Embodiment 11:

Adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 19mm.

Its central angle d of agitating plate 602 is 41 °.

The agitating plate of each impeller is adjacent that staggered angle f is 20 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 40 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 19mm.

The central angle d ' of agitating plate 702 is 41 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 20 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 40 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 19mm.

The central angle d of agitating plate 802 " be 41 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 20 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 60 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 19mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 4.2: 4.2: 1.

Preferred embodiment:

According to the foregoing description, adopt following technical parameter to improve embodiment one:

In described first stirring system 6:

The inwall of the material scraping plate 603 and the first chamber shell 202 is tangent, and leaves the safety clearance of 6mm.

Its central angle d of agitating plate 602 is 30 °.

The agitating plate of each impeller is adjacent that staggered angle f is 15 ° between the agitating plate of impeller.

The angle g that agitating plate 602 and perpendicular and material scraping plate are 603 is 10 °.

In described second stirring system 7:

The inwall of the material scraping plate 703 and the second chamber shell 203 is tangent, and leaves the safety clearance of 6mm.

The central angle d ' of agitating plate 702 is 30 °.

The agitating plate of each impeller is adjacent that staggered angle f ' is 15 ° between the agitating plate of impeller.

The angle g ' that agitating plate 702 and perpendicular and material scraping plate are 703 is 10 °.

In described the 3rd stirring system 8:

The inwall of the material scraping plate 803 and the second chamber shell 207 is tangent, and leaves the safety clearance of 6mm.

The central angle d of agitating plate 802 " be 30 °.

The agitating plate of each impeller is adjacent staggered angle f between the agitating plate of impeller " be 15 °.

The angle g that agitating plate 802 and perpendicular and material scraping plate are 803 " be 45 °.

Material scraping plate on arbitrary blade of arbitrary impeller of second stirring system 7 is also tangent near a side of second rotating shaft 502 with first rotating shaft 501, and leaves the safety clearance of 6mm.

The rotating ratio of first rotating shaft 501, second rotating shaft 502 and the 3rd rotating shaft 503 is 3.5: 3.5: 1.

Claims

1, a kind of horizontal solid-liquid mixer, it is characterized in that, comprise feed system (201), the first chamber shell (202), the second chamber shell (203), the 3rd chamber shell (207), outer casing (204), first rotating shaft (501), second rotating shaft (502), the 3rd rotating shaft (503), first stirring system (6), second stirring system (7), the 3rd stirring system (8), material transfer system (200) and discharge system (209); The described first chamber shell (202) and the second chamber shell (203) are two hollow cylinder structures that intersect, described the 3rd chamber shell (207) is positioned at the bottom of the first chamber shell (202), the second chamber shell (203), and interconnect with both by material transfer system (200), the axle center of three cavitys is parallel to each other, and is positioned at the inside of outer casing (204);

Described first chamber shell (202) inside is formed with first cavity (205), second chamber shell (203) inside is formed with second cavity (206), the 3rd chamber shell (207) inside is formed with the 3rd cavity (208), and described first cavity (205), second cavity (206) and the 3rd cavity (208) are interconnected;

Described first rotating shaft (501) is positioned at first cavity (205) inside, and by its center of circle;

Described second rotating shaft (502) is positioned at second cavity (206) inside, and by its center of circle;

Described the 3rd rotating shaft (503) is positioned at the 3rd cavity (208) inside, and by its center of circle;

Described first stirring system (6) is connected in first rotating shaft (501), and rotates thereupon;

Described second stirring system (7) is connected in second rotating shaft (502), and rotates thereupon;

Described the 3rd stirring system (8) is connected in the 3rd rotating shaft (503), and rotates thereupon.

2, a kind of horizontal solid-liquid mixer as claimed in claim 1, it is characterized in that, described first stirring system (6) is one group of impeller that is connected in first rotating shaft (501), described each impeller comprises 2～4 blades that include stirring piece (602) and material scraping plate (603), and interlobate angular interval equates;

One end of described stirring piece (602) is connected in the rotating shaft (501), and the other end is connected with material scraping plate (603), and this material scraping plate (603) is tangent with the inwall of the first chamber shell (202), and leaves the safety clearance of 2mm～20mm;

Described second stirring system (7) is one group of impeller that is connected in second rotating shaft (502), and described each impeller comprises 2～4 blades that include agitating plate (702) and material scraping plate (703), and interlobate angular interval equates;

One end of described stirring piece (702) is connected in the rotating shaft (502), and the other end is connected with material scraping plate (703), and this material scraping plate (703) is tangent with the inwall of the second chamber shell (203), and leaves the safety clearance of 2mm～20mm;

Described the 3rd stirring system (8) is one group of impeller that is connected in the 3rd rotating shaft (503), and described each impeller comprises 2～4 blades that include agitating plate (802) and material scraping plate (803), and interlobate angular interval equates;

One end of described stirring piece (802) is connected in the rotating shaft (503), and the other end is connected with material scraping plate (803), and this material scraping plate (803) is tangent with the inwall of the 3rd chamber shell (207), and leaves the safety clearance of 2mm～20mm.

3, a kind of horizontal solid-liquid mixer as claimed in claim 2 is characterized in that, the stirring piece of each impeller of described first stirring system (6) is adjacent staggered 0 °～45 ° angles between the stirring piece of impeller;

The stirring piece of each impeller of described second stirring system (7) is adjacent staggered 0 °～45 ° angles between the stirring piece of impeller;

The stirring piece of each impeller of described the 3rd stirring system (8) is adjacent staggered 0 °～45 ° angles between the stirring piece of impeller.

4, a kind of horizontal solid-liquid mixer as claimed in claim 3 is characterized in that, described stirring piece (602) is a sector structure, and its internal diameter equates that with rotating shaft (501) external diameter its external diameter is the poor of first chamber shell (202) internal diameter and material scraping plate (603) thickness;

The center of circle angle of described fan-shaped stirring piece (602) is 10 °～45 °;

Described stirring piece (702) is a sector structure, and its internal diameter equates that with rotating shaft (502) external diameter its external diameter is the poor of second chamber shell (203) internal diameter and material scraping plate (703) thickness;

The center of circle angle of described fan-shaped stirring piece (702) is 10 °～45 °;

Described stirring piece (802) is a sector structure, and its internal diameter equates that with rotating shaft (503) external diameter its external diameter is the poor of the 3rd chamber shell (207) internal diameter and material scraping plate (803) thickness;

The center of circle angle of described fan-shaped stirring piece (702) is 10 °～45 °.

5, a kind of horizontal solid-liquid mixer as claimed in claim 4 is characterized in that, described material scraping plate (603) is a sector structure, and its internal diameter equates that with stirring piece (602) external diameter its external diameter equates with first chamber shell (202) internal diameter;

Described material scraping plate (603) equates with the center of circle angle of its stirring piece that is connected (602);

Described material scraping plate (703) is a sector structure, and its internal diameter equates that with stirring piece (702) external diameter its external diameter equates with second chamber shell (203) internal diameter;

Described material scraping plate (703) equates with the center of circle angle of its stirring piece that is connected (702);

Described material scraping plate (803) is a sector structure, and its internal diameter equates that with stirring piece (802) external diameter its external diameter equates with the 3rd chamber shell (207) internal diameter;

Described material scraping plate (803) equates with the center of circle angle of its stirring piece that is connected (802).

6, a kind of horizontal solid-liquid mixer as claimed in claim 5, it is characterized in that, described material scraping plate (603) is in same plane with perpendicular, and described stirring piece (602) becomes 0 °～45 ° angles, preferred 30 ° of angles with perpendicular with material scraping plate (603);

Described material scraping plate (703) is in same plane with perpendicular, and described stirring piece (702) becomes 0 °～45 ° angles, preferred 30 ° of angles with perpendicular with material scraping plate (703);

Described material scraping plate (803) is in same plane with perpendicular, and described stirring piece (802) becomes 20 °～65 ° angles, preferred 45 ° of angles with perpendicular with material scraping plate (803).

7, a kind of horizontal solid-liquid mixer as claimed in claim 6 is characterized in that, the interval of respectively organizing between the impeller of described first stirring system (6) equates;

The interval of respectively organizing between the impeller of described second stirring system (7) equates;

The interval of respectively organizing between the impeller of described the 3rd stirring system (8) equates;

The impeller of the impeller of described first stirring system (6) and second stirring system (7) is staggered, be distributed with the impeller of one group of second stirring system (7) between the impeller of wantonly two groups of adjacent first stirring systems (6), and this first stirring system (6) impeller equates with the spacing of this second stirring system (7) impeller with spacing and another first stirring system (6) impeller of second stirring system (7) impeller;

Material scraping plate on arbitrary blade of arbitrary impeller of described second stirring system (7) is also tangent near a side of second rotating shaft (502) with first rotating shaft (501), and leaves the safety clearance of 2mm～20mm.

8, a kind of horizontal solid-liquid mixer as claimed in claim 7 is characterized in that, the radius of the described first chamber shell (202) and the second chamber shell (203) equates;

The diameter of described the 3rd chamber shell (207) is first chamber shell (202) radius, first rotating shaft (501) radius and second chamber shell (203) the diameter sum;

Described first rotating shaft (501) and second rotating shaft (502) are done and are relatively rotated;

The rotating ratio of described first rotating shaft (501), second rotating shaft (502) and the 3rd rotating shaft (503) is 2.2: 2.2: 1～4.6: 4.6: 1.

9, a kind of horizontal solid-liquid mixer as claimed in claim 8, it is characterized in that, the described outer casing (204) and the first chamber shell (202) comprise that further the position thereon and pass wherein the first chamber door (2020), so that when opening the described first chamber door (2020), expose first cavity (205); The described outer casing (204) and the second chamber shell (203) further comprise the position thereon and pass wherein the second chamber door (2030), so that when opening the described second chamber door (2030), expose second cavity (206);

Described outer casing (204) and the 3rd chamber shell (207) further comprise the position thereon and pass wherein the 3rd chamber door (2070), so that when opening described the 3rd chamber door (2070), expose the 3rd cavity (208).

10, a kind of horizontal solid-liquid mixer as claimed in claim 9, it is characterized in that described feed system (201) comprises feeding-in solid body mouth (2011), liquid inlet opening (2012), the first additive charging aperture (2013), the second additive charging aperture (2014);

Described feeding-in solid body mouth (2011) and liquid inlet opening (2012) are adjacent to be arranged on described outer casing (204) end face, and penetrate described outer casing (204) and the first chamber shell (202), the second chamber shell (203) respectively, be communicated with described first cavity (205) and second cavity (206);

The described first additive charging aperture (2013), the second additive charging aperture (2014) are arranged on described outer casing (204) end face, and penetrate the described outer casing (204) and the first chamber shell (202), are communicated with described first cavity (205);

Described material transfer system (200) is arranged on the outer casing (204), and penetrate outer casing (204), the first chamber shell (202), the second chamber shell (203) and the 3rd chamber shell (207), be communicated with first cavity (205), second cavity (206) and the 3rd cavity (208);

Described discharge system (209) is arranged on described outer casing (204) bottom surface, and penetrates described outer casing (204) and the 3rd chamber shell (207), is communicated with described the 3rd cavity (208).