CN101837274A - Multidirectional stirring-type two-cavity hybrid reaction chamber and method thereof - Google Patents
Multidirectional stirring-type two-cavity hybrid reaction chamber and method thereof Download PDFInfo
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- CN101837274A CN101837274A CN200910047815A CN200910047815A CN101837274A CN 101837274 A CN101837274 A CN 101837274A CN 200910047815 A CN200910047815 A CN 200910047815A CN 200910047815 A CN200910047815 A CN 200910047815A CN 101837274 A CN101837274 A CN 101837274A
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Abstract
The invention relates to a multidirectional stirring-type two-cavity hybrid reaction chamber and a method thereof. The two-cavity hybrid reaction chamber comprises a feed system, an outer shell, a discharge system, a first cavity shell, a second cavity shell, a first cavity, a second cavity, a first rotating shaft, a second rotating shaft, a first stirring system and a second stirring system, wherein the first cavity shell and the second cavity shell are intersected and both in a hollow cylinder structure; the first cavity and the second cavity, the axes of which are parallel to each other, are respectively formed in the first cavity shell and the second cavity shell; the first rotating shaft and the second rotating shaft are respectively positioned at the center of circle of the two cavities; the first stirring system and the second stirring system are respectively positioned on the two rotating shafts and rotate along with the two rotating shafts; the second stirring system is an set of impeller composed of a rotating shaft, a scraper and a rotator; and the rotator is in a ring transformer structure, the rotating shafts pass through the hollow interior of the rotator, and the outer circumference of the ring is provided with a concave-convex gear, thereby forming an impeller structure and performing the action of stirring.
Description
Technical field
The present invention relates to a kind of two-cavity hybrid reaction chamber, particularly a kind of multidirectional stirring-type two-cavity hybrid reaction chamber belongs to the mechanical mixing equipment field.
The invention still further relates to a kind of method that adopts multidirectional stirring-type two-cavity hybrid reaction chamber to mix.
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 agitation mixer and stirring mixing method are disclosed, this equipment 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 equipment 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 apparatus 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 equipment, 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 equipment 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 apparatus and mixed method are disclosed, this equipment 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 equipment respectively, utilize the shunting of each material, mix, yet the said equipment are not suitable for mixing of powder and high viscosity solidliquid mixture.
Simultaneously in the Chinese patent 200410090534.4, disclose the horizontal mixing apparatus that a kind of inside has stirring vane, powder and liquid from the top and bottom injection device of a side of horizontal mixing apparatus, utilize blade to mix respectively then.Need in having full-bodied solidliquid mixture, to add simultaneously liquid and pressed powder yet this equipment 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 apparatus, yet the said equipment 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
One object of the present invention is to provide a kind of multidirectional stirring-type two-cavity hybrid reaction chamber, 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.
Another object of the present invention is to provide a kind of mixed method that adopts multidirectional stirring-type two-cavity hybrid reaction chamber to mix, solidliquid mixture and pressed powder, liquid, additive etc. evenly can be mixed according to a certain ratio by this method, be specially adapted to the even mixing of high solidliquid mixture of viscosity and pressed powder, liquid, additive.
A kind of multidirectional stirring-type two-cavity hybrid reaction chamber disclosed in this invention comprises feed system, the first chamber shell, the second chamber shell, outer casing, first rotating shaft, second rotating shaft, first stirring system, second stirring system and discharge system.
The described first chamber shell and the second chamber shell are two hollow cylinder structures that intersect, and both axle center are parallel to each other, and are positioned at the inside of outer casing.Shell inside, described first chamber is formed with first cavity, and shell inside, second chamber is formed with second cavity, and described first cavity and second cavity are interconnected.
Described first rotating shaft is positioned at first inside cavity, and by its center of circle.Described first stirring system is connected in first rotating shaft, and rotates thereupon.
Described first stirring system is one group of impeller that is connected in first rotating shaft, and described each impeller comprises 2～4 blades that include agitating plate and material scraping plate, and interlobate angular interval equates.One end of described agitating plate is connected in the rotating shaft, and the other end is connected with material scraping plate, and the inwall of this material scraping plate and the first chamber shell is tangent, and leaves the safety clearance of 2mm～20mm.
Described agitating plate is a sector structure, and its center of circle angle is 10 °～45 °, and its internal diameter equates that with the rotating shaft external diameter its external diameter is the poor of the first chamber shell internal diameter and material scraping plate thickness.
Described material scraping plate 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 its internal diameter equates that with the agitating plate external diameter its external diameter equates with the first chamber shell internal diameter.
Described material scraping plate and perpendicular are in same plane, and described agitating plate becomes 0 °～45 ° angles with perpendicular with material scraping plate, preferred 30 ° of angles.
The agitating plate of each impeller of described first stirring system 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 equates.
Described second rotating shaft is positioned at second inside cavity, and by its center of circle.Described second stirring system is connected in second rotating shaft, and rotates thereupon.
Described second stirring system is one group of impeller that is connected in second rotating shaft, described each impeller includes rotating shaft, material scraping plate and whirligig, one end of described rotating shaft is connected in the rotating shaft, the other end is connected with material scraping plate, the inwall of this material scraping plate and the second chamber shell is tangent, and leaves the safety clearance of 2mm～20mm.
Described rotating shaft is the center of circle with second rotating shaft, and around its rotation, described whirligig is enclosed within on the rotating shaft, and is the center of circle with it, around its rotation.
Described whirligig is an annulus deformable body structure, and the inner circular of its hollow is used for by rotating shaft, and the circumference in its ring outside is provided with concavo-convex gear, thereby forms blade wheel structure, plays stirring action.
Described rotating shaft is that a vertical cross section is approximate rectangular column structure, its external diameter equates with the whirligig internal diameter, one side of described approximate rectangular cross section joins with second rotating shaft, and the length of described rotating shaft is the poor of the second chamber shell internal diameter and material scraping plate thickness, the second rotating shaft radius.
Described rotating shaft, material scraping plate and perpendicular are in same plane.
The interval of respectively organizing between the impeller of described second stirring system equates.
The impeller of the impeller of described first stirring system and second stirring system is staggered, be distributed with the impeller of one group of second stirring system between the impeller of wantonly two groups of first adjacent stirring systems, and this first stirring system impeller equates with the spacing of this second stirring system impeller with spacing and another first stirring system impeller of the second stirring system impeller.The material scraping plate on the rotating shaft of arbitrary impeller of described second stirring system and first rotating shaft are tangent near a side of second rotating shaft, and leave the safety clearance of 2mm～20mm.
The radius ratio of the described first chamber shell and the second chamber shell is 1: 1～1: 2.2.
The rotating ratio of described first rotating shaft, second rotating shaft and whirligig is 1: 1: 1～8.6: 1: 4.3.
The described outer casing and the first chamber shell further comprise the position thereon and pass wherein the first chamber door, so that when opening the described first chamber door 0, expose first cavity.The described outer casing and the second chamber shell further comprise the position thereon and pass wherein the second chamber door, so that when opening the described second chamber door, expose second cavity.
Described feed system comprises feeding-in solid body mouth, liquid inlet opening, the first additive charging aperture, the second additive charging aperture, is positioned at the premix material inlet of outer casing bottom.
Described feeding-in solid body mouth and liquid inlet opening 2 are adjacent to be arranged on the described outer casing end face, and penetrate described outer casing and the first chamber shell, the second chamber shell respectively, are communicated with described first cavity and second cavity.
The described first additive charging aperture, the second additive charging aperture are arranged on the described outer casing end face, and penetrate the described outer casing and the first chamber shell, are communicated with described first cavity.
Described discharge system is arranged on the described outer casing bottom surface, and penetrates the described outer casing and the second chamber shell, is communicated with described second cavity.
A kind of mixed method that adopts multidirectional stirring-type two-cavity hybrid reaction chamber to mix disclosed by the invention comprises following steps:
Step 1: enter first cavity and second cavity from the premix material inlet input premix material of outer casing bottom, and under the rotation stirring action of first stirring system and second stirring system, be evenly distributed on first cavity and second inside cavity.
Step 2: enter first inside cavity from described feeding-in solid body mouth input pressed powder, under the rotation stirring action of first stirring system, described pressed powder mixes with the premix material is full and uniform.
Step 3: simultaneously, enter second inside cavity from described liquid inlet opening input gas, liquid or gas-liquid mixture, under the rotation stirring action of second stirring system, 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 and second stirring system, 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 of each impeller of first stirring system and second stirring system and whirligig, to first cavity and the transmission of the second cavity rear portion.
The material scraping plate of each impeller of first stirring system and second stirring system and respectively material that adheres on the first chamber shell inwall, the second chamber shell inwall being struck off is to mix once more.
Step 5: enter first cavity and second cavity from the first additive charging aperture, 3 input additives, under the rotation stirring action of first stirring system and second stirring system, 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 of each impeller of first stirring system and second stirring system and whirligig, to first cavity and the transmission of the second cavity rear portion.
The material scraping plate of each impeller of first stirring system and second stirring system and respectively material that adheres on the first chamber shell inwall, the second chamber shell inwall being struck off is to mix once more.
Step 6: enter first cavity and second cavity from second additive charging aperture input additive, under the rotation stirring action of first stirring system and second stirring system, the full and uniform mixing of described additive and mixed material obtains mixture.
Described mixture is under the effect of the agitating plate of each impeller of first stirring system and second stirring system and whirligig, to first cavity and the transmission of the second cavity rear portion.
The material scraping plate of each impeller of first stirring system and second stirring system and respectively material that adheres on the first chamber shell inwall, the second chamber shell inwall being struck off is to mix once more.
Step 7: by the agitating plate of each impeller of first stirring system and second stirring system and the rotation stirring and the gravity effect of whirligig, described mixture is exported from discharge system.
Utilize said apparatus and method, the premix material inlet input premix material from the outer casing bottom under the stirring of first stirring system and second stirring system, is evenly distributed on first cavity and second inside cavity.Add pressed powder and liquid enters first cavity and second cavity from feeding-in solid body mouth and liquid inlet opening this moment simultaneously, pressed powder evenly mixes in first inside cavity and premix material, liquid evenly mixes in second inside cavity and premix material, thereby avoided between the pressed powder that adds and the liquid because the secondary aggregation that mixing brings.First stirring system and second stirring system 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 and the second additive charging aperture 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 invention 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, utilization of the present invention 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 multidirectional stirring-type two-cavity hybrid reaction chamber of the present invention.
Fig. 2 is the viewgraph of cross-section of multidirectional stirring-type two-cavity hybrid reaction chamber of the present invention along the A-A ' of Fig. 1.
Fig. 3 is the side view of the agitating plate of multidirectional stirring-type two-cavity hybrid reaction chamber of the present invention and material scraping plate, whirligig.
Fig. 4 is the viewgraph of cross-section along the B-B ' of Fig. 1 of multidirectional stirring-type two-cavity hybrid reaction chamber of the present invention.
Fig. 5 a, 5b, 5c, 5d are the schematic diagrames of stagger angle relation between each impeller of one group of adjacent impeller of multidirectional stirring-type two-cavity hybrid reaction chamber of the present invention.
The specific embodiment
According to claim of the present invention and the disclosed content of summary of the invention, technical scheme of the present invention is specific as follows described.
Embodiment one:
A kind of multidirectional stirring-type two-cavity hybrid reaction chamber comprises as the lower part:
According to Fig. 1 and Fig. 2:
A kind of multidirectional stirring-type two-cavity hybrid reaction chamber comprises feed system 201, the first chamber shell 202, the second chamber shell 203, outer casing 204, first rotating shaft 501, second rotating shaft 502, first stirring system 6, second stirring system 7 and discharge system 209.
The described first chamber shell 202 and the second chamber shell 203 are two hollow cylinder structures that intersect, and both axle center are parallel to each other, and are 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, and described first cavity 205 and second cavity 206 are interconnected.
According to Fig. 2:
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 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.
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.
According to Fig. 2:
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, described each impeller includes rotating shaft 701, material scraping plate 702 and whirligig 703, one end of described rotating shaft 701 is connected in the rotating shaft 502, the other end is connected with material scraping plate 702, the inwall of this material scraping plate 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 2mm～20mm.
Described rotating shaft 701 is the center of circle with second rotating shaft 502, and around its rotation, described whirligig 703 is enclosed within on the rotating shaft 701, and is the center of circle with it, around its rotation.
Described whirligig 703 is annulus deformable body structures, and the inner circular of its hollow is used for by rotating shaft 701, and the circumference in its ring outside is provided with concavo-convex gear, thereby forms blade wheel structure, plays stirring action.
Described rotating shaft 701 is that a vertical cross section is approximate rectangular column structure, its external diameter equates with whirligig 703 internal diameters, one side of described approximate rectangular cross section joins with second rotating shaft 502, and the length of described rotating shaft 701 is the poor of the second chamber shell, 203 internal diameters and material scraping plate 702 thickness, second rotating shaft, 502 radiuses.
Described rotating shaft 701, material scraping plate 702 are in same plane with perpendicular.
According to Fig. 2 and Fig. 5 a, 5b, 5c, 5d:
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.
According to Fig. 3:
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 whirligig 703 is rotary blades of the gear-like of a hollow, and hollow space wherein is circular, is used for by rotating shaft 701 and is that the axle center is rotated with this rotating shaft 701.When rotating shaft 701 was center of circle rotation with second rotating shaft 502, driving the whirligig 703 that connects on it was center of circle rotation with second rotating shaft 502 also.So whirligig 703 is when self rotating around rotating shaft 701, also further around second rotating shaft, 502 rotations.
According to Fig. 2 and Fig. 4:
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 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 and Fig. 2:
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, is positioned at the premix material inlet of outer casing 204 bottoms.
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 discharge system 209 is arranged on described outer casing 204 bottom surfaces, and penetrates the described outer casing 204 and the second chamber shell 203, is communicated with described second cavity 206.
According to Fig. 2:
The radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1～1: 2.2.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 whirligig 703 is 1: 1: 1～8.6: 1: 4.3.
A kind of mixed method that adopts multidirectional stirring-type two-cavity hybrid reaction chamber to mix disclosed by the invention comprises following steps:
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.
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.
According to Fig. 2 and Fig. 4:
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 whirligig 703, to first cavity 206 and the transmission of second cavity, 207 rear portions.
The material scraping plate 603 and 702 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.
According to Fig. 1 and Fig. 2
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 whirligig 703, to first cavity 206 and the transmission of second cavity, 207 rear portions.
The material scraping plate 603 and 702 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 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 whirligig 703, to first cavity 206 and the transmission of second cavity, 207 rear portions.
The material scraping plate 603 and 702 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 7: by the agitating plate 602 of each impeller of first stirring system 6 and second stirring system 7 and the rotation stirring and the gravity effect of whirligig 703, described mixture is from discharge system 209 outputs.
According to Fig. 4, 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 and whirligig 703 effects thereof, 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 respectively by impeller 60012 and impeller 70012 and whirligig 703 stirrings thereof, 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 is added the pressed powder that advances in second batch of solidliquid mixture of impeller 70012 and whirligig 703 stirrings thereof increases and the content minimizing of the liquid that interpolation is advanced, 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 by first group of impeller 6001 and 7001 and whirligig 703 back kicks transport to second group of chamber, since then, from the first additive charging aperture, 2013 input additives, the solidliquid mixture that is mixed with additive second group of impeller 6002 and 7002 and whirligig 703 effects under, described in the past mode is carried out mixing at random repeatedly and is separated at random, so that additive evenly distributes.Subsequently the gained solidliquid mixture by second impeller sets 6002 and 7002 and whirligig 703 back kicks transport to the 3rd chamber, to mix mutually with additive from the input of 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.
Wherein, whirligig 703 is rotary blades of the gear-like of a hollow, and hollow space wherein is circular, is used for by rotating shaft 701 and is that the axle center is rotated with this rotating shaft 701.When rotating shaft 701 was center of circle rotation with second rotating shaft 502, driving the whirligig 703 that connects on it was center of circle rotation with second rotating shaft 502 also.Gu whirligig 703 is when self rotating around rotating shaft 701, also further around second rotating shaft, 502 rotations.So this whirligig 703 not only can be so that material, can also make that material is that the center of circle moves in a circle in second cavity, 206 inside with second rotating shaft 502 along second rotating shaft, 502 axially-movables.Whirligig 703 and bring omnibearing various material movement.
Wherein, the radius ratio of the described first chamber shell 202 and the second chamber shell 203 is that the rotating ratio of 1: 1～1: 2.2 and described first rotating shaft 501, second rotating shaft 502 and whirligig 703 is 1: 1: 1～8.6: 1: 4.3, promptly the volume and the material rotating speed of second cavity, 206 inside are equal to or greater than first cavity, at this moment, second cavity 206 mainly plays storing mixture, and slowly stir, increase 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.If do not need the above-mentioned reaction time, then the radius ratio of the first chamber shell 202 and the second chamber shell 203 can be made as 1: 1 and its rotating ratio of described first rotating shaft 501 and second rotating shaft 502 was made as 1: 1.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 3mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1.2.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 1.2: 1.
Described second rotating shaft 502 is 1.1: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 5mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1.3.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 2.0: 1.
Described second rotating shaft 502 is 1.3: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 7mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1.4.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 2.8: 1.
Described second rotating shaft 502 is 1.5: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 9mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1.5.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 3.6: 1.
Described second rotating shaft 502 is 1.7: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 11mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1.6.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 4.4: 1.
Described second rotating shaft 502 is 2.1: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 12mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1.7.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 5.2: 1.
Described second rotating shaft 502 is 2.5: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 13mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1.8.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 6.0: 1.
Described second rotating shaft 502 is 2.9: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 15mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1.9.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 6.8: 1.
Described second rotating shaft 502 is 3.3: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 17mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 2.0.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 7.6: 1.
Described second rotating shaft 502 is 3.7: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 19mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 2.1.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 8.4: 1.
Described second rotating shaft 502 is 4.1: 1 with the rotating speed of whirligig 703.
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 702 and the second chamber shell 203 is tangent, and leaves the safety clearance of 6mm.
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 radius ratio of the described first chamber shell 202 and the second chamber shell 203 is 1: 1.5.
The rotating ratio of described first rotating shaft 501 and second rotating shaft 502 is 4.2: 1.
Described second rotating shaft 502 is 2.2: 1 with the rotating speed of whirligig 703.
Foregoing is exemplifying of specific embodiments of the invention, for the wherein not equipment of detailed description and structure, should be understood to take existing common apparatus in this area and universal method to be implemented.
Claims (10)
1. multidirectional stirring-type two-cavity hybrid reaction chamber, it is characterized in that, comprise feed system (201), the first chamber shell (202), the second chamber shell (203), outer casing (204), first rotating shaft (501), second rotating shaft (502), first stirring system (6), second stirring system (7) and discharge system (209);
The described first chamber shell (202) and the second chamber shell (203) are two hollow cylinder structures that intersect, both axle center are parallel to each other, and be positioned at the inside of outer casing (204), at the two inner corresponding first cavity (205) and second cavity (206) that is interconnected that form respectively;
Described first rotating shaft (501) and second rotating shaft (502) lay respectively at first cavity (205) and second cavity (206) inside accordingly, and accordingly respectively by the two center of circle;
Described first stirring system (6) is one group and is connected in first rotating shaft (501) and the impeller that thereupon rotates that described each impeller comprises 2～4 blades that include stirring piece (602) and material scraping plate (603), and interlobate angular interval equates;
Described second stirring system (7) is one group and is connected the impeller that second rotating shaft (502) is gone up and rotated thereupon that described each impeller includes rotating shaft (701), material scraping plate (702) and has the whirligig (703) of concavo-convex gear.
2. a kind of multidirectional stirring-type two-cavity hybrid reaction chamber as claimed in claim 1, it is characterized in that, one end of described rotating shaft (701) is connected in the rotating shaft (502), the other end is connected with material scraping plate (702), this material scraping plate (702) is tangent with the inwall of the second chamber shell (203), and leaves the safety clearance of 2mm～20mm;
Described rotating shaft (701) is the center of circle with second rotating shaft (502), and around its rotation, described whirligig (703) is enclosed within on the rotating shaft (701), and is the center of circle with it, around its rotation.
3. a kind of multidirectional stirring-type two-cavity hybrid reaction chamber as claimed in claim 2, it is characterized in that, described whirligig (703) is an annulus deformable body structure, the inner circular of its hollow is used for by rotating shaft (701), the circumference in its ring outside is provided with concavo-convex gear, thereby the formation blade wheel structure plays stirring action;
Described rotating shaft (701) is that a vertical cross section is approximate rectangular column structure, its external diameter equates with whirligig (703) internal diameter, one side of described approximate rectangular cross section joins with second rotating shaft (502), and the length of described rotating shaft (701) is the poor of second chamber shell (203) internal diameter and material scraping plate (702) thickness, second rotating shaft (502) radius.
4. a kind of multidirectional stirring-type two-cavity hybrid reaction chamber as claimed in claim 3, it is characterized in that, one end of described stirring piece (602) is connected in the rotating shaft (501), the other end is connected with material scraping plate (603), 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 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 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).
5. a kind of multidirectional stirring-type two-cavity hybrid reaction chamber as claimed in claim 4, 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 rotating shaft (701), material scraping plate (702) are in same plane with perpendicular.
6. a kind of multidirectional stirring-type two-cavity hybrid reaction chamber as claimed in claim 5 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 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.
7. a kind of multidirectional stirring-type two-cavity hybrid reaction chamber as claimed in claim 6, it is characterized in that, 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 (702) on the rotating shaft (701) of arbitrary impeller of described second stirring system (7) is 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 multidirectional stirring-type two-cavity hybrid reaction chamber as claimed in claim 7 is characterized in that, the radius ratio of the described first chamber shell (202) and the second chamber shell (203) is 1: 1～1: 5.5; Described first rotating shaft (501) is done with second rotating shaft (502) and is relatively rotated;
The rotating ratio of described first rotating shaft (501), second rotating shaft (502) and whirligig (703) is 1: 1: 1～8.6: 1: 4.3.
9. a kind of multidirectional stirring-type two-cavity hybrid reaction chamber 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 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 discharge system (209) is arranged on described outer casing (204) bottom surface, and penetrates the described outer casing (204) and the second chamber shell (203), is communicated with described second cavity (206).
10. a mixed method that adopts multidirectional stirring-type two-cavity hybrid reaction chamber as claimed in claim 9 to mix is characterized in that, 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) bottom, 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 (206) inside;
Step 2: enter first cavity (205) inside from described feeding-in solid body mouth (2011) input pressed powder, 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 gas, 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 whirligig (703), to first cavity (206) and the transmission of second cavity (207) rear portion;
Strike off the material that adheres on first chamber shell (202) inwall, second chamber shell (203) inwall respectively the material scraping plate (603) of each impeller of first stirring system (6) and second stirring system (7) and (702), to mix once more;
Step 5: enter first cavity (206) and second cavity (207) from the first additive charging aperture (2013) input additive, 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 whirligig (703), to first cavity (206) and the transmission of second cavity (207) rear portion;
Strike off the material that adheres on first chamber shell (202) inwall, second chamber shell (203) inwall respectively the material scraping plate (603) of each impeller of first stirring system (6) and second stirring system (7) and (702), to mix once more;
Step 6: enter first cavity (206) and second cavity (207) from the second additive charging aperture (2014) input additive, 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 whirligig (703), to first cavity (206) and the transmission of second cavity (207) rear portion;
Strike off the material that adheres on first chamber shell (202) inwall, second chamber shell (203) inwall respectively the material scraping plate (603) of each impeller of first stirring system (6) and second stirring system (7) and (702), to mix once more;
Step 7: by the agitating plate (602) of each impeller of first stirring system (6) and second stirring system (7) and the rotation stirring and the gravity effect of whirligig (703), described mixture is exported from discharge system (209).
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| CN200910047815A CN101837274A (en) | 2009-03-19 | 2009-03-19 | Multidirectional stirring-type two-cavity hybrid reaction chamber and method thereof |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107427795A (en) * | 2015-03-25 | 2017-12-01 | 高露洁-棕榄公司 | For mixing and distributing the apparatus and method of fluid |
| CN112912475A (en) * | 2018-04-04 | 2021-06-04 | 埃科金苏斯有限责任公司 | Treatment vessels for forming fuel compositions and related systems and methods |
| US11879106B2 (en) | 2014-10-30 | 2024-01-23 | EcoGensus LLC | Process for forming a solid fuel composition from mixed solid waste |
-
2009
- 2009-03-19 CN CN200910047815A patent/CN101837274A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11879106B2 (en) | 2014-10-30 | 2024-01-23 | EcoGensus LLC | Process for forming a solid fuel composition from mixed solid waste |
| CN107427795A (en) * | 2015-03-25 | 2017-12-01 | 高露洁-棕榄公司 | For mixing and distributing the apparatus and method of fluid |
| CN107427795B (en) * | 2015-03-25 | 2021-07-02 | 高露洁-棕榄公司 | Apparatus and method for mixing and dispensing fluids |
| CN112912475A (en) * | 2018-04-04 | 2021-06-04 | 埃科金苏斯有限责任公司 | Treatment vessels for forming fuel compositions and related systems and methods |
| US11781083B2 (en) | 2018-04-04 | 2023-10-10 | EcoGensus LLC | Process vessel for forming fuel compositions and related systems and methods |
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Application publication date: 20100922 |