CN202212120U - Conical tri-rotor continuous mixing unit with triangularly arranged rotors - Google Patents

Conical tri-rotor continuous mixing unit with triangularly arranged rotors Download PDF

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Publication number
CN202212120U
CN202212120U CN2011201957040U CN201120195704U CN202212120U CN 202212120 U CN202212120 U CN 202212120U CN 2011201957040 U CN2011201957040 U CN 2011201957040U CN 201120195704 U CN201120195704 U CN 201120195704U CN 202212120 U CN202212120 U CN 202212120U
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CN
China
Prior art keywords
mixing
rotor
rotors
section
conical
Prior art date
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Expired - Fee Related
Application number
CN2011201957040U
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Chinese (zh)
Inventor
王克俭
郭冰
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Beijing University of Chemical Technology
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Beijing University of Chemical Technology
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Priority to CN2011201957040U priority Critical patent/CN202212120U/en
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Publication of CN202212120U publication Critical patent/CN202212120U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/39Plasticisers, homogenisers or feeders comprising two or more stages a first extruder feeding the melt into an intermediate location of a second extruder
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/465Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft each shaft comprising rotor parts of the Banbury type in addition to screw parts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/48Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
    • B29B7/485Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws with three or more shafts provided with screws
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/48Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
    • B29B7/488Parts, e.g. casings, sealings; Accessories, e.g. flow controlling or throttling devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/582Component parts, details or accessories; Auxiliary operations for discharging, e.g. doors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/60Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/72Measuring, controlling or regulating
    • B29B7/728Measuring data of the driving system, e.g. torque, speed, power, vibration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476Systems, i.e. flow charts or diagrams; Plants
    • B29B7/7485Systems, i.e. flow charts or diagrams; Plants with consecutive mixers, e.g. with premixing some of the components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476Systems, i.e. flow charts or diagrams; Plants
    • B29B7/7495Systems, i.e. flow charts or diagrams; Plants for mixing rubber
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/82Heating or cooling
    • B29B7/826Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/285Feeding the extrusion material to the extruder
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/365Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using pumps, e.g. piston pumps

Abstract

The utility model relates to a conical tri-rotor continuous mixing unit with triangularly arranged rotors, which mainly comprises a mixing portion and a discharging portion and can adopt a single-stage or double-stage form. The mixing portion mainly comprises a feeding device, a barrel, the conical rotors, a heating and cooling device and a transmission. The central lines of the three conical rotors for mixing are positioned on edges of a triangular pyramid when the conical rotors are mounted, and the conical rotors are triangularly arranged in a section. The peripheral contour of each rotor for mixing is decreased from large to small to be conical, and each rotor for mixing is provided with a feeding section and a mixing section, wherein each feeding section is a spiral conveying structure. Viewed from a conical surface perpendicular to the peripheral contour of each rotor, the structure of the mixing section of each rotor is typically in a cam shape, an S shape, a four-edge shape or the like. When the single-stage form is adopted, pressure is generated at the tail ends of the rotors by the aid of the spiral structures to convey materials to a head. When the double-stage form is adopted, mixing materials enter a screw extruder at a next stage through a valve to generate pressure for conveying materials to the head. The head with a proper cavity is adopted to realize granulating or forming in both of the forms, and a melt pump can be connected into the front of the head to further increase the pressure. The speeds of the three rotors can be the same or different, a plurality of shearing, stretching and kneading areas are formed when the rotors run, the materials among the rotors are exchanged more frequently, plasticizing, melting and dispersing performances of equipment are improved effectively, processing time is shortened, and yield is improved. The mixing unit can be used for technological processes of mixing, granulating and the like for processing rubber, coating, propellant, explosive, paper pulp, plastics, food, medicines, fodder and the like.

Description

The taper triple-spool continuous mixing unit of rotor rounded projections arranged
Technical field
The present invention relates to the taper triple-spool continuous mixing unit of rotor rounded projections arranged, can be used for the technical process such as mixing and granulation in the processing such as rubber, coating, propellant, explosive, paper pulp, plastics, food, pharmacy, feed.
Background technology
Mixing is decision high molecular products performance-critical process procedure, and particularly high viscous-elastic materials such as rubber being seemed is even more important.All even the stablizing that material is mixing is the key of guaranteeing the polymer product quality.Realize the evenly mixing technical equipment of mixing main dependence, comprise mill, banbury, two-rotor continuous mixer and screw extruder etc.In the industry, screw extruder is mainly used in the plasticizing processing of plastics and food and thermoplastic elastomer (TPE), and other three kinds then are mainly used in the mixing of component complex materials such as rubber, coating, explosive and propellant.Mill and banbury belong to batch-mixed equipment, and not only efficient is low, and are difficult to reach the different identical mixing quality of material in batches.
Two-rotor continuous mixer has combined the excellent mixed characteristic of banbury, also with continuous running, on industrial mass manufacture, is used widely.It mainly partly is made up of machine barrel, rotor, device for discharging etc.Mixing chamber on the machine barrel is that two that each other connect, cross sections are circular hole, and material receives the effect of shearing, pulverizing, kneading and the mixing of rotor in mixing chamber.Non-counter-rotating intermeshing rotor rotated mainly is made up of feeding section, mixing section and discharging section.The rotor feeding section is as the twin-screw of two non-engagements, and under the promotion of rotor feeding section screw thread, the material by charge door adds arrives mixing section.The rotor mixing section surface screw thread that helical angle has nothing in common with each other, stagger arrangement is arranged, material is in this fusion, mixing, plasticizing.Device for discharging can be controlled the open degree of Dump gate, reaches the purpose of control material time of staying in mixing chamber.
Patent 200910250492.9 is developed the conical three-screw rod extruder of rounded projections arranged, and three screw rod rounded projections arranged form three and mediate district and a center.Relative two screw rods extruder, three-screw extruder has the positive conveyance characteristic of fricting shearing and a plurality of region of engagements, and material and screw rod have bigger contact area.Mixing fully, heat transmitting is good, melt capacity is big, exhaust capacity is good and temperature control is better, and have lower energy consumption.The screw rod tail diameter increases the bearing capacity that has also increased screw rod; Feeding section screw channel volume is big, is prone to add the bulk density powder of larger volume; The discharge zone screw diameter is little, and peripheral speed is less, and the shearing of generation is lower, and frictional heat is also less, fire damage dangerous little; The screw channel volume reduces along extruding direction gradually, and material obtains compression gradually, thereby makes screw channel be full of material sooner, guarantees material plasticizing gently continuously; Under same production capacity, back pressure can be lower.
Similarly, on the basis of birotor mixing roll, adopt three cone rotors to form new mixing roll.Three roots rotors are arranged in parallel, and form three and mediate district and a center, and mixing fully, heat transmitting is good, melt capacity is big, exhaust capacity is good and temperature control is better; Not only improve output and energy-conservation, mixed effect also can obviously improve, and can also be applicable to temperature-sensitive materials such as powder and PVC.
Summary of the invention
Be different from traditional double rotor mixing roll, continuous mixer of the present invention adopts three cone rotors to be triangularly arranged, and forms the mixing structure of taper triple-spool, like Fig. 1.Wherein mixing part mainly is made up of feeding device, machine barrel, cone rotor, heating-cooling device and transmission device.Mixing have three with cone rotor, and its center line is positioned on the rib of triangular pyramid during installation, is triangularly arranged in the section.Each mixing rotor diameter profile is tapered by reducing greatly, has feeding section and mixing section, and feeding section adopts screw conveying structure; From seeing perpendicular to the rotor outline conical surface, the mixing section structure presents typical rotor characteristics such as cam-shaped, S shape or tetragonous rotor type.
Further, be continuous mixing, must the mass transport that mix be carried out granulation or moulding to head, promptly removing kneading part exceptionally also needs the discharge part.Like this, triple-spool continuous mixing unit partly is made up of mixing part and discharge.The complete unit that for this reason forms can be a single-order, also can be two rank.
Single-order triple-spool continuous mixer is exactly that rotor is made up of non-engaging spiro rod feeding section and mixing rotor section and screw rod discharge zone successively; Material added continuously with mixing and through the transportation section pressure is discharged to head and carries out granulation or moulding, the head cavity structure depends on the outlet article shape.Be to improve outlet discharge pressure, but connection gear pump also before the head.
The triple-spool continuous mixing unit such as the Fig. 1 on two rank mainly contain mixing part and discharge and partly form.In first rank non-engaging spiro rod feeding section and mixing rotor section are manufactured an integral body, material is added continuously and is mixing, is discharged to second rank through the adjustable discharge valve of aperture endways.The aperture control discharge rates and the degree of filling that forms second rank of valve, build-up pressure, the mixing intensity of change mixer.Second rank can be screw extruders, adopt to be fit to the screw-rod structure that fused materials adds, and carry out granulation or moulding through screw rod transmission to head, and the head cavity structure depends on the outlet article shape.Be to improve outlet discharge pressure, but connection gear pump also before the head.
During the operation of triple-spool mixing roll, add material at charge door, to mixing rotor section, making full use of effectively, rotor structure carries out mixing repeatedly and plasticates through helical feed.Because three rotors are arranged, the strong drawing zone between rotor is multiplied with mediating to distinguish.Rotor mixing section of the present invention is taper, and is big near the feeding section diameter, little near the discharge zone diameter.Correspondingly, the machine barrel that comprises rotor also is to be combined to form by three cones.Except that conventional rotors the variation of circumferential and axial structural cycle property, the cone rotor diameter will produce axial compression kneading effect and strengthen axial conveying effect from large to small, promote mixed material to move downstream.Therefore can obviously improve melting effect and improve output, have the effect of energy-saving and emission-reduction.
Simultaneously, the cone rotor tail diameter increases, and feeding quantity increases, and has also improved output; Increased the rotor bearing capacity, gear and bearing long service life help arranging thrust bearing and gear; Big near the feeding section volume, the easy bulk density powder that adds larger volume also helps the heat conduction, more is prone to realization to material heating or cooling; Volume near discharge zone is little, and peripheral speed is less, and the shearing of generation is lower, and frictional heat is also less, fire damage dangerous little; Along with rotor diameter reduces gradually, material obtains compression gradually, thereby makes screw channel be full of material sooner, guarantees that material is gently mixing continuously; Under same production capacity, back pressure can be lower.Like this, such mixing roll also can be used for temperature-sensitive materials such as powder and PVC.
Description of drawings
Fig. 1 is the taper triple-spool continuous mixing unit structural representation of rotor rounded projections arranged
The 1-motor, 2-slows down and distributor box, the 3-machine barrel, the 4-feeding device, the 5-heater, the 6-cone rotor, 7-rotor cooling device, the 8-motor, the 9-reduction box, the 10-machine barrel, the 11-heater, the 12-screw rod, the 13-head, the 14-discharge valve, 15-connects cylindrical shell.
Fig. 2 adopts the sectional schematic diagram of cam face for the rotor mixing section
Fig. 3 adopts the sectional schematic diagram of S shape rotor for the rotor mixing section
Fig. 4 adopts the sectional schematic diagram of tetragonous rotor for the rotor mixing section
The specific embodiment
This case study on implementation is the taper triple-spool continuous mixing unit on two rank.
The taper triple-spool continuous mixing unit of cone rotor rounded projections arranged can be that taper triple-spool continuous mixer connecting screw rod extruder is formed, and sees Fig. 1.Mixing part mainly comprises: motor 1, slow down and distributor box 2, and machine barrel 3, feeding device 4, heater 5, cone rotor 6, rotor cooling device 7 is formed.The screw rod extruding part comprises: motor 8, and reduction box 9, machine barrel 10, heater 11, screw rod 12, machine head port mould 13 is formed.Connect through cylindrical shell 15 between mixing part and the screw rod extruding part, wherein be provided with the adjustable discharge valve 14 of aperture.The transmission device of motor 1, deceleration and distributor box 2 component devices.
Mixing part is with three cone rotors, and its center line is positioned on the rib of triangular pyramid during installation, is triangularly arranged in the section.Each mixing rotor diameter profile is tapered by reducing greatly, has feeding section and mixing section, and feeding section adopts screw conveying structure; From seeing perpendicular to the rotor outline conical surface, the mixing section structure presents typical rotor characteristics such as cam-shaped, S shape or tetragonous rotor type.
The operation principle of this continuous mixing unit is: motor 1 drives the rotation of reduction box power shaft, carries out the distribution of moment of torsion and rotating speed in the reduction box 2 and rotates in machine barrel through three cone rotors 6 of three output shafts drives.Three cone rotors 6 lean on terminal cooling system to regulate internal temperature.Rotor has non-meshing spiral transportation section and rotor-type mixing section, and is installed in the machine barrel 3, and machine barrel is regulated external temperature under heater 5 effects.Material adds in the machine barrel 3 through feeding device 4, arrives mixing rotor section through helical feed.The heat that dependence is imported into from machine barrel, the shearing of rotor, stretching and extruding kneading effect, material plastifies and mixes.Mixing sufficient material through discharge valve 14 be connected cylindrical shell 15 and get into the screw rod extruding parts, build-up pressure is extruded through head 13 under the helical feed effect, carries out granulation or moulding.For further improving pressure, can insert Melt Pump before the head.
Three rotor mixing sections are non-engagements, therefore can be with speed or differential, and the direction of rotation of three rotors can be carried out various combination.For this reason, can adopt integrated deceleration and distributor box, also can adopt separate type reduction box and distributor box to realize the rotor motion combination, need consider that simultaneously the cone rotor axis is the requirement that cone angle is arranged.The rotor mixing section can make full use of various typical mixing rotor structures, like the cam-shaped of Fig. 2, the S shape of Fig. 3 and the tetragonous rotor type of Fig. 4 etc.
Because three rotors are arranged, the strong drawing zone between rotor, strong shear zone and strong crush zone are multiplied, between rotor the material exchange more frequent, make material plasticating in screw rod, homogenizing, the number of times of shearing is multiplied; This structure is mixing mutually compound with cone rotor axial compression kneading effect with triple-spool; The plasticating of equipment, fusion and dispersive property have more effectively been improved; Shorten process time, had the characteristics of energy-saving and emission-reduction, also can be used for the mixing of temperature-sensitive materials such as powder and PVC.

Claims (2)

1. the taper triple-spool continuous mixing unit of rotor rounded projections arranged mainly partly is made up of mixing part and discharge, can adopt single-order or two rank form; Wherein mixing part mainly is made up of feeding device, machine barrel, cone rotor, heating-cooling device and transmission device, it is characterized in that: mixing have three with cone rotor, and its center line is positioned on the rib of triangular pyramid during installation, is triangularly arranged in the section.
2. the taper triple-spool continuous mixing unit of rotor rounded projections arranged according to claim 1 is characterized in that: each mixing rotor diameter profile is tapered by reducing greatly, has feeding section and mixing section, and feeding section adopts screw conveying structure; From seeing perpendicular to the rotor outline conical surface, the mixing section structure presents cam-shaped, S shape or and the typical rotor characteristics of tetragonous rotor type.
CN2011201957040U 2011-06-10 2011-06-10 Conical tri-rotor continuous mixing unit with triangularly arranged rotors Expired - Fee Related CN202212120U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011201957040U CN202212120U (en) 2011-06-10 2011-06-10 Conical tri-rotor continuous mixing unit with triangularly arranged rotors

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011201957040U CN202212120U (en) 2011-06-10 2011-06-10 Conical tri-rotor continuous mixing unit with triangularly arranged rotors

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Publication Number Publication Date
CN202212120U true CN202212120U (en) 2012-05-09

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102228818A (en) * 2011-06-10 2011-11-02 北京化工大学 Continuous mixing unit with three tapered rotors in triangular arrangement
CN104608281A (en) * 2015-01-29 2015-05-13 中国纺织科学研究院 Dynamic mixer
CN114847503A (en) * 2022-05-19 2022-08-05 中国农业大学 Multi-component mixed double-input screw extrusion equipment and extrusion processing method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102228818A (en) * 2011-06-10 2011-11-02 北京化工大学 Continuous mixing unit with three tapered rotors in triangular arrangement
CN104608281A (en) * 2015-01-29 2015-05-13 中国纺织科学研究院 Dynamic mixer
CN104608281B (en) * 2015-01-29 2017-07-14 中国纺织科学研究院 Dynamic mixer
CN114847503A (en) * 2022-05-19 2022-08-05 中国农业大学 Multi-component mixed double-input screw extrusion equipment and extrusion processing method

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120509

Termination date: 20130610