CN2353445Y - Rotary pulsating superfine-microparticle powder disintegrator - Google Patents

Rotary pulsating superfine-microparticle powder disintegrator Download PDF

Info

Publication number
CN2353445Y
CN2353445Y CN 99204774 CN99204774U CN2353445Y CN 2353445 Y CN2353445 Y CN 2353445Y CN 99204774 CN99204774 CN 99204774 CN 99204774 U CN99204774 U CN 99204774U CN 2353445 Y CN2353445 Y CN 2353445Y
Authority
CN
China
Prior art keywords
wing
stator
rotor disk
tooth
rotary
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 99204774
Other languages
Chinese (zh)
Inventor
王力民
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wang Limin
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN 99204774 priority Critical patent/CN2353445Y/en
Application granted granted Critical
Publication of CN2353445Y publication Critical patent/CN2353445Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Crushing And Pulverization Processes (AREA)

Abstract

The utility model relates to a rotary pulsating powder pulverizer for superfine particulates, composed of a shell, a rotor disk, a stator disk, an inlet tube, an outlet tube, a drive shaft, a machine cover, rotor wing teeth and stator blade teeth, wherein, the drive shaft (13) is glidingly connected with a center hole of the shell (3), and a shaft end of the drive shaft is fixedly connected with the rotor disk (1) with the wing teeth (6, 7, 8); the inner end surface of the machine cover (14) is fixedly connected with the stator disk (2) also with wing teeth (9, 10, 11). The wing teeth of the rotor disk and the wing teeth of the stator disk engaged according to certain spaces fix the machine cover on the end surface of the shell and connect the inlet tube (4) with the outlet tube (5) to form a whole body. The utility model improves pulverizing uniformity, simultaneously raises work efficiency, and enhances adaptability in various industrial circles.

Description

Rotary pulsive superfine powder mixing grinder
A kind of pulverizer, especially rotary pulsive superfine powder mixing grinder, what relate to is the technical field of mechanical pulverizer.
Blade of a sword formula pulverizer in the known technology, abrasive disk type pulverizer, its weak point are that noise is big, efficient is low, grinding particle size is inhomogeneous, function singleness, and narrow application range is unsuitable for industrial needs such as chemistry, mine, food, medicine especially.
The purpose of this utility model is to provide a kind of rotary pulsive superfine powder mixing grinder, mainly is to improve the uniformity of pulverizing, and increases work efficiency, and strengthens its adaptability in many industrial circles.
Above-mentioned purpose is achieved through the following technical solutions:
Form overall structure by housing, rotor disk, stator dish, inlet tube, outlet, power transmission shaft, cover, rotor wing tooth and stator wing tooth.
Power transmission shaft (13) is slidingly connected in the centre bore of housing (3), the fixedly connected rotor disk (1) that has wing tooth (6,7,8) of its axle head, again in the fixedly connected stator dish (2) that has wing tooth (9,10,11) of the inner face of cover (14), make its rotor disk wing tooth and stator disk wing tooth, at a certain distance after the engagement, cover is fixedly connected on the housing end face, establishes inlet tube (4), outlet (5), promptly constitute whole.
On the side of rotor disk (1) and stator dish (2), respectively from interior circle beginning gradually outwards at a certain distance, uniform 3~6 row's wing teeth (6,7,8) and (9,10,11) of line-spacing.
Wing tooth on rotor disk (1) and the stator dish (2), be to distribute by certain displacement concentric circles, the distance of adjacent foil between cog on concentric circles, be less than or equal to the wing facewidth degree on the next concentric circles of outer direction, its shift value, be that any a pair of adjacent foil between cog channel cross-section is in open position, the channel cross-section of the wing between cog that any one is relative is in closed condition.
The wing tooth of rotor disk (1) and stator dish (2) (6,7,8,9,10,11) is an arcuation, and its center line overlaps with axial line.
Inlet tube (4) is connected the center, outer face of cover (14), and outlet (5) is connected the top of housing (3).
Thus, many advantages of the present utility model show.
When this equipment of utilization carries out the even phase process of other industry of petroleum emulsification, owing to there is fluid pulse speed, change with the liquid flow path direction, make the even efficient of changing process mutually improve greatly, and the size of emulsion droplet also diminishes, improve fluctuation velocity, also just improved material dispersed speed and dust dispersion quality, because the turbulence type fluctuation velocity is to cause a grain broken major reason in the emulsion process.So equipment is by a circulation, just can obtain to stablize, the ultramicro oil water emulsion (drop is about 5 microns) of homogeneous, dispersion.This equipment of that is to say can be used as Continuous Emulsifier, need not be the pre-emulsification of each component.
Accompanying drawing of the present utility model and drawing explanation are:
Fig. 1 is the structure cutaway view of rotary pulsive superfine powder mixing grinder;
Fig. 2 is a stator disk wing tooth horizontal layout cutaway view;
Fig. 3 is a rotor disk wing tooth horizontal layout cutaway view;
Fig. 4 is the stator disk wing tooth horizontal layout cutaway view of another form;
Fig. 5 is rotor disk and stator disk wing tooth engagement cutaway view;
Fig. 6 is that wing tooth engagement back passage is opened, closed schematic diagram;
Fig. 7 is that wing tooth engagement back passage is opened, closed schematic diagram;
The utility model is described in further detail below in conjunction with drawings and Examples:
The ultrafine dust pulverizing machine is a rotary pulse equipment, it is by having wing tooth 6,7,8,9,10,11 rotor disk 1 and stator dish 2 constitute, wing tooth is arranged by concentric circumferences, each dish all has certain displacement when upward distributing by concentric circles, the distance of the adjacent foil between cog on concentric circles, be less than or equal wing facewidth degree on the next concentric circles of outer direction, pterion on one or several concentric circles in rotor or the stator dish, its shift value will guarantee when any a pair of adjacent foil between cog channel cross-section is in open position on rotor disk and the stator dish, and the channel cross-section of the phase adjacency pair wing between cog that distributes along concentric circles is in closed condition.In order to reach this point, the channel cross-section axle on some concentric circles is coincided with other wing tooth axles that are close on concentric circles that coil together.Also can make the shift value of wing tooth, guarantee that the ratio between the number of channels on each concentric circles equals non-integer or equals non-odd number.
Since in the utility model on concentric circles the distance of adjacent foil between cog be less than or equal to wing facewidth degree on the next concentric circles of outer direction, and the wing tooth on one or several concentric circles in rotor or the stator dish, its shift value will guarantee: when any a pair of adjacent foil between cog channel cross-section was in open position on rotor disk and the stator dish, the channel cross-section of the wing between cog of the phase adjacency pair that distributes along concentric circles was in closed condition.Therefore, it has guaranteed the increase of vertical flow stream velocity fluctuation velocity, and when rotor and stator were in any relative position, laterally the direction of liquid stream can change.The change of liquid flow path direction makes and separates in the slit of solid particle between stator dish and rotor disk that still solid particle is pulverized tempestuously in this slit, and is big more as particle size at this moment, and when the liquid flow path direction changed, their were with regard to easy more separation.The solid that some particle is big more, the time that rests in the strong pulverizing district is long more, and the particle that reaches standard is taken out of rapidly by liquid stream and is pulverized the district.This process has guaranteed that each particle is crushed to needed granularity quickly, so the particle of pulverizing is extremely even, has reduced and has pulverized meticulous possibility, thereby reduced loss (fine grained can be crushed to 3~5 microns).This equipment must be with the surperficial plated with gold emery of rotor dish, to strengthen its abrasion resistance when pulverizing all kinds of ore.
Fig. 5,6, the 7th, stator and rotor arrangements schematic diagram, the structure of this equipment, form by rotor disk 1, stator dish 2, housing 3, inlet tube 4 and outlet 5 on it, on rotor and stator dish, install rotor disk wing tooth parts 6,7,8 and stator wing tooth 9,10,11 according to concentrically ringed mode.
The sectional axis that runs through axle center, hole, cross section and tooth wing 9,10 that must accomplish tooth wing 10 coincides.
Material is through import 4, deliver on the rotating disc 1, because the rotation of rotor disk produces centrifugal force, the material that is stirred is by stator and rotor disk 1,2, move to outer rim along running through the cross section mouth between the tooth wing that is positioned on the concentric circles line, the effect of tooth wing forms turbulation, and because the effect between stator dish 1 and rotor disk 2 tooth wings forms fluctuating velocity, thereby has eliminated the dry run phenomenon of logistics.As long as observe the condition of a≤b, just can obtain the circumscribed minibreak of logistics.At this moment separation (pulverizing) effect maximum.Mixtures of materials arrives the rotor plate edge, just gets rid of by outlet 5.

Claims (5)

1, a kind of rotary pulsive superfine powder mixing grinder, by housing, rotor disk, the stator dish, inlet tube, outlet, power transmission shaft, cover, rotor wing tooth and stator wing tooth are formed, it is characterized in that: a power transmission shaft (13) is slidingly connected in the centre bore of housing (3), the fixedly connected wing tooth (6 that has of its axle head, 7,8) rotor disk (1), again in the fixedly connected wing tooth (9 that has equally of the inner face of cover (14), 10,11) stator dish (2), after rotor disk wing tooth and stator disk wing tooth mesh at a certain distance, cover is fixedly connected on the housing end face, connect inlet tube (4) and outlet (5), promptly constitute whole.
2, rotary pulsive superfine powder mixing grinder according to claim 1, it is characterized in that: on the side of rotor disk (1) and stator dish (2), begin gradually outwards at a certain distance from interior garden respectively, line-spacing uniform 3~6 row wing teeth (6,7,8) and (9,10,11).
3, rotary pulsive superfine powder mixing grinder according to claim 1 and 2, it is characterized in that: the wing tooth on rotor disk (1) and the stator dish (2), be to distribute by the certain displacement concentric circles, the i.e. distance of adjacent foil tooth on concentric circles, it is the wing facewidth degree that is less than or equal on the next concentric circles of outer direction, its shift value is that any a pair of adjacent foil between cog channel cross-section is in open position, and the channel cross-section of any one adjacent foil between cog is in closed condition.
4, rotary pulsive superfine powder mixing grinder according to claim 1 and 2 is characterized in that: the wing tooth of rotor disk (1) (6,7,8) all is an arcuation with the wing tooth (9,10,11) of stator dish (2), and its center line overlaps with axial line.
5, rotary pulsive superfine powder mixing grinder according to claim 1 and 2 is characterized in that: inlet tube (4) is connected the center, outer face of cover (14), and outlet (5) is connected the top of housing (3).
CN 99204774 1999-02-26 1999-02-26 Rotary pulsating superfine-microparticle powder disintegrator Expired - Fee Related CN2353445Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 99204774 CN2353445Y (en) 1999-02-26 1999-02-26 Rotary pulsating superfine-microparticle powder disintegrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 99204774 CN2353445Y (en) 1999-02-26 1999-02-26 Rotary pulsating superfine-microparticle powder disintegrator

Publications (1)

Publication Number Publication Date
CN2353445Y true CN2353445Y (en) 1999-12-15

Family

ID=33999476

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 99204774 Expired - Fee Related CN2353445Y (en) 1999-02-26 1999-02-26 Rotary pulsating superfine-microparticle powder disintegrator

Country Status (1)

Country Link
CN (1) CN2353445Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101873015A (en) * 2010-07-02 2010-10-27 无锡轻大食品装备有限公司 Stator and rotor structure of dismountable high-shearing pulverizing equipment
CN101892604A (en) * 2010-07-06 2010-11-24 湖北工业大学 Combined impeller millstone pulping method and device
CN109248751A (en) * 2017-07-14 2019-01-22 广州新致晟环保科技有限公司 Sludge crusher and the method for being crushed sludge using it

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101873015A (en) * 2010-07-02 2010-10-27 无锡轻大食品装备有限公司 Stator and rotor structure of dismountable high-shearing pulverizing equipment
CN101873015B (en) * 2010-07-02 2012-07-18 无锡轻大食品装备有限公司 Stator and rotor structure of dismountable high-shearing pulverizing equipment
CN101892604A (en) * 2010-07-06 2010-11-24 湖北工业大学 Combined impeller millstone pulping method and device
CN109248751A (en) * 2017-07-14 2019-01-22 广州新致晟环保科技有限公司 Sludge crusher and the method for being crushed sludge using it

Similar Documents

Publication Publication Date Title
US4874136A (en) Pulp refining apparatus
CN110394082A (en) A kind of impeller assembly and solid and liquid mixing equipment using the component
CN111249941B (en) Impeller assembly for dispersing solid in liquid and solid-liquid mixing equipment using same
JPS59173596A (en) Device for pumping up pulp
CN87103124A (en) Vertical mill
WO2006133577A1 (en) Centrifugal pump
CN2353445Y (en) Rotary pulsating superfine-microparticle powder disintegrator
DE3751292T2 (en) IMPROVED PUMP DESIGN.
CN203678460U (en) Double-shaft-driven wet type medium stirring grinder
CN114433311A (en) High-efficient sand mill centrifugation discharge system of intelligence
CN2414835Y (en) Pulsed superfine particle pulverizing machine
CN1305872A (en) Rotary pulsive superfine powder mixing grinder
CN202155314U (en) Centrifugal horizontal cage type powder separator with forced vortex
DE19840344A1 (en) Classifying wheel for a centrifugal air classifier
CN218423185U (en) Efficient cooling ultrafine grinder
CN2897430Y (en) Accelerating crusher of circulating air-flow impeller
JP5794564B2 (en) Stirrer
CA2415858C (en) Double disk refiner, stock inducer therefor and method of refining low consistency stock
CN2442745Y (en) High-shearing viscolizer
CN2385792Y (en) Rotation superfine viscolizing emusifying device
CN209379103U (en) A kind of coating material production sand mill
CN115007010A (en) Adjustable throttle high-lift gas-liquid mixing pump
CN209423744U (en) A kind of sand mill for coating material production
CN2799075Y (en) Vertical wet-process super grinder
CN209696804U (en) A kind of dispersion and emulsion device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C53 Correction of patent for invention or patent application
COR Change of bibliographic data

Free format text: CORRECT: PATENTEE ADDRESS; FROM: 806, TOWER A, GUANZHUANGJINGTONGXINCHENGZIWEI APT., CHAOYANG DISTRICT, BEIJING CITY, 100024 TO: BAOZHUANGYINSHUA FACTORY, HARBIN CITY, NO. 11, GONGDIAN ROAD, NANGANG DISTRICT, HARBIN CITY, HEILONGJIANG PROVINCE, 150080

CP03 Change of name, title or address

Address after: 150080, Nangang District, Heilongjiang, Harbin No. 11 circuit, Harbin packaging printing factory Wang Liquan transferred to Wang Limin

Patentee after: Wang Limin

Address before: 100024 Beijing Chaoyang District city Guanzhuang Beijing Metro Ziwei apartment A block 806

Patentee before: Wang Limin

C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee