CN206493471U - A kind of plastic raw materials high efficient mixer - Google Patents

A kind of plastic raw materials high efficient mixer Download PDF

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Publication number
CN206493471U
CN206493471U CN201720134999.8U CN201720134999U CN206493471U CN 206493471 U CN206493471 U CN 206493471U CN 201720134999 U CN201720134999 U CN 201720134999U CN 206493471 U CN206493471 U CN 206493471U
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China
Prior art keywords
buffer
hybrid chamber
raw materials
helical
filter bores
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Expired - Fee Related
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CN201720134999.8U
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Chinese (zh)
Inventor
曾庆志
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China Tech Moral Novel Material Co Ltd Of Shenzhen
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China Tech Moral Novel Material Co Ltd Of Shenzhen
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  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

The utility model provides a kind of plastic raw materials high efficient mixer, for mixing plastic raw materials, according to the fill process of plastic raw materials, sequentially pass through charging aperture, gradient hybrid chamber, air blast hybrid chamber, stirring hybrid chamber and discharging chamber, the gradient hybrid chamber is into 25 45 ° of cylinder chamber with ground, be disposed with from top to bottom inside it on 36 buffer boards parallel to the ground, the buffer board and filter bores be set, and on different buffer board filter bores it is of different sizes;The discharge outlet of the gradient hybrid chamber is identical with the charging aperture of air blast hybrid chamber.

Description

A kind of plastic raw materials high efficient mixer
Technical field
The utility model is related to a kind of mixer technology field, and in particular to B01F15 fields.
Background technology
The process that the making of plastic material is general is as follows:Proportionally match somebody with somebody raw material, be then blended at a high speed, powdery and grain Heated and extruded into extruder by feed opening after the material mixing of shape, the plastic strip of extrusion is cooled down through water-carrying groove, cold But shearing cutting granulating is carried out afterwards, and the filtering through sifting out after pelletizing claims by filtering out for falling short of specifications, then by storage silo Packed after amount.In above process, dispensing must be stirred when blending at a high speed could enter extruder, not so bad Rate will be improved.In recent years, as product containing filler systems gradually increases, stability and phase of these products to the glue containing filler Capacitive requires higher.
Simultaneously in plastics industry field, recovered material and the raw material newly bought, the motion speed of existing mixer are often mixed Degree and direction change little, are easily caused material layering, influence mixing uniformity.For this problem, the utility model is provided A kind of plastic raw materials high efficient mixer.
Utility model content
In view of the above-mentioned problems, the utility model provides a kind of plastic raw materials high efficient mixer, it is former for mixing plastics Material, according to the fill process of plastic raw materials, sequentially passes through charging aperture, gradient hybrid chamber, air blast hybrid chamber, stirring hybrid chamber and discharging Chamber.
The gradient hybrid chamber is that into 25-45 ° of cylinder chamber, 3-6 are disposed with from top to bottom inside it with ground Filter bores are set on buffer board parallel to the ground, the buffer board, and on different buffer boards filter bores it is of different sizes;It is described The discharge outlet of gradient hybrid chamber is identical with the charging aperture of air blast hybrid chamber;
The air blast hybrid chamber is provided with the column construction of air-blast device, and the interior intracavitary of the air blast hybrid chamber for bottom The Baltimore groove of rotation is provided with, the Baltimore groove has double-deck spill piece, respectively outer layer spill piece and internal layer spill piece, and institute State and be respectively arranged with outer filter hole and internal layer filter bores, and the diameter in outer filter hole on outer layer spill piece and internal layer spill piece Filter bore dia for internal layer 1.1-1.3 times;
The stirring hybrid chamber is the cylindrical structural that intracavitary has rotary shaft vertically, and its lower end is provided with discharging chamber.
As a kind of embodiment of the present utility model, rotary buffer device is vertically arranged with stirring hybrid chamber, it is described Rotary shaft is upper and lower to be vertically arranged with two groups of helical-blades, respectively the first helical-blade and the second helical-blade, and the second helical-blade respectively Length be 1.5-2 times of the first helical-blade length.
As a kind of embodiment of the present utility model, the first buffer subsystem is provided with the top of the rotary shaft, and it is described The second buffer subsystem and the 3rd buffer subsystem are provided with the inwall for stirring hybrid chamber, second buffer subsystem is arranged on the first buffer subsystem And first between helical-blade, the 3rd buffer subsystem is arranged between the first helical-blade and the second helical-blade;
The angle in first buffer subsystem and straight up direction is in 30-60 degree;
Second buffer subsystem and the 3rd buffer subsystem and the angle of vertically downward direction are in 30-60 degree;
Hole is set on first buffer subsystem, the second buffer subsystem and the 3rd buffer subsystem.
As a kind of embodiment of the present utility model, the length of second helical-blade is the first helical-blade length 1.5-1.8 again.
As a kind of embodiment of the present utility model, 4 buffer boards are provided with the gradient hybrid chamber, from up to It is respectively the first buffer board, the second buffer board, the 3rd buffer board and the 4th buffer board down.
As a kind of embodiment of the present utility model, the first buffer board, the second buffer board, the 3rd buffer board and the 4th are slow The first filter bores, the second filter bores, the 3rd filter bores and the 4th filter bores are respectively arranged with punching.
It is used as a kind of embodiment of the present utility model, first filter bores, the second filter bores, the 3rd filter bores and The aperture ratio of four filter bores is 1.5:1.3:1.2:1.
As a kind of embodiment of the present utility model, the angle in first buffer subsystem and straight up direction is 50 Degree.
As a kind of embodiment of the present utility model, the angle of second buffer subsystem and vertically downward direction is 45 Degree.
As a kind of embodiment of the present utility model, the angle of the 3rd buffer subsystem and vertically downward direction is 35 Degree.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art Or the accompanying drawing used required in description of the prior art is briefly described, it should be apparent that, drawings in the following description are only It is some embodiments of the present utility model, for those of ordinary skill in the art, is not paying the premise of creative work Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1:The schematic diagram of plastic raw materials high efficient mixer
Fig. 2:The schematic diagram of first buffer board
Fig. 3:The schematic diagram of outer layer spill piece
Symbol description:
Charging aperture 1, gradient hybrid chamber 2, air blast hybrid chamber 3 stirs hybrid chamber 4, discharging chamber 5;
Buffer board 21, filter bores 211, air-blast device 31, Baltimore groove 32, outer layer spill piece 321, internal layer spill piece 322, outside Layer filter bores 3211, rotary shaft 41, the first helical-blade 411, the second helical-blade 412, the first buffer subsystem 6, the second buffer subsystem 61, the Three buffer subsystems 62, the first buffer board 211, the second buffer board 212, the 3rd buffer board 213, the 4th buffer board 214.
Embodiment
In view of the above-mentioned problems, the utility model provides a kind of plastic raw materials high efficient mixer, it is former for mixing plastics Material, according to the fill process of plastic raw materials, sequentially passes through charging aperture, gradient hybrid chamber, air blast hybrid chamber, stirring hybrid chamber and goes out Expect chamber,
The gradient hybrid chamber is that into 25-45 ° of cylinder chamber, 3-6 are disposed with from top to bottom inside it with ground Filter bores are set on buffer board parallel to the ground, the buffer board, and on different buffer boards filter bores it is of different sizes;It is described The discharge outlet of gradient hybrid chamber is identical with the charging aperture of air blast hybrid chamber;
The air blast hybrid chamber is provided with the column construction of air-blast device, and the interior intracavitary of the air blast hybrid chamber for bottom The Baltimore groove of rotation is provided with, the Baltimore groove has double-deck spill piece, respectively outer layer spill piece and internal layer spill piece, and institute State and be respectively arranged with outer filter hole and internal layer filter bores, and the diameter in outer filter hole on outer layer spill piece and internal layer spill piece Filter bore dia for internal layer 1.1-1.3 times;
The stirring hybrid chamber is the cylindrical structural that intracavitary has rotary shaft vertically, and its lower end is provided with discharging chamber.
Mixer:
Mixer is that the machinery for uniformly mixing two or more material is set using mechanical force and gravity etc. It is standby.During mixing, material contact surface area can also be increased, to promote chemical reaction;Physical change can also be accelerated. Conventional mixer be divided into gas and low-viscosity (mobile) liquid mixer, medium-high viscosity liquid and paste mixer, powdery with it is granular The major class of solid material mixing machinery four.
Gas and low-viscosity (mobile) liquid blender feature are simple in construction, and no-rotary parts, and Maintenance and Repair amount is small, energy consumption It is low.This kind of mixing machinery is divided into four kinds of airflow stirring, pipeline mixing, jet mixing and forced circulation mixing etc. again.Mixer is matched somebody with somebody Part mainly has wear resistant alloy material manufacture, including high-speed stirred scraper, stirring wing, abrasion-proof backing block, mixing arm, stirring shovel, planet Shovel, stirring colter, stirring rod, raker stirrer etc..The mixing machinery of middle and high viscosity liquid and paste typically there is strong shearing to make With.
Common mixer has:Colter mixer, spiral ribbon mixer, Agravicmixer, V-Mixer, double helix cone Shape mixer, high low-velocity liquid mixer, planetary power mixer etc..
As a kind of embodiment of the present utility model, rotary buffer device is vertically arranged with the stirring hybrid chamber, The rotary shaft is upper and lower to be vertically arranged with two groups of helical-blades, respectively the first helical-blade and the second helical-blade, and the second spiral shell respectively The length of vane is 1.5-2 times of the first helical-blade length.
As a kind of embodiment of the present utility model, the first buffer subsystem is provided with the top of the rotary shaft, and it is described The second buffer subsystem and the 3rd buffer subsystem are provided with the inwall for stirring hybrid chamber, second buffer subsystem is arranged on the first buffer subsystem And first between helical-blade, the 3rd buffer subsystem is arranged between the first helical-blade and the second helical-blade;
The angle in first buffer subsystem and straight up direction is in 30-60 degree;
Second buffer subsystem and the 3rd buffer subsystem and the angle of vertically downward direction are in 30-60 degree;
Hole is set on first buffer subsystem, the second buffer subsystem and the 3rd buffer subsystem.
As a kind of embodiment of the present utility model, the length of second helical-blade is the first helical-blade length 1.5-1.8 again.
As a kind of embodiment of the present utility model, 4 buffer boards are provided with the gradient hybrid chamber, from up to It is respectively the first buffer board, the second buffer board, the 3rd buffer board and the 4th buffer board down.
As a kind of embodiment of the present utility model, the first buffer board, the second buffer board, the 3rd buffer board and the 4th are slow The first filter bores, the second filter bores, the 3rd filter bores and the 4th filter bores are respectively arranged with punching.
It is used as a kind of embodiment of the present utility model, first filter bores, the second filter bores, the 3rd filter bores and The aperture ratio of four filter bores is 1.5:1.3:1.2:1.
As a kind of embodiment of the present utility model, the angle in first buffer subsystem and straight up direction is 50 Degree.
As a kind of embodiment of the present utility model, the angle of second buffer subsystem and vertically downward direction is 45 Degree.
As a kind of embodiment of the present utility model, the angle of the 3rd buffer subsystem and vertically downward direction is 35 Degree.
As shown in Figure 1-2, the utility model plastic raw materials high efficient mixer is described:A kind of plastic raw materials are efficiently mixed Conjunction machine, for mixing plastic raw materials, according to the fill process of plastic raw materials, sequentially pass through charging aperture 1, gradient hybrid chamber 2, Air blast hybrid chamber 3, stirring hybrid chamber 4 and discharging chamber 5,
The gradient hybrid chamber 2 is that into 25-45 ° of cylinder chamber, 3-6 are disposed with from top to bottom inside it with ground The size of filter bores in filter bores 211, and different buffer boards is set on buffer board 21 parallel to the ground, the buffer board 21 It is different;The discharge outlet of the gradient hybrid chamber 2 is identical with the charging aperture of air blast hybrid chamber 3;
The air blast hybrid chamber 3 is that bottom is provided with the column construction of air-blast device 31, and the air blast hybrid chamber 3 is interior Intracavitary is provided with the Baltimore groove 32 of rotation, and the Baltimore groove has double-deck spill piece, and respectively outer layer spill piece 321 and internal layer is recessed Outer filter hole 3211 and internal layer mistake are respectively arranged with shape piece 322, and the outer layer spill piece 321 and internal layer spill piece 322 Filter opening, and 1.1-1.3 times of a diameter of internal layer filtering bore dia in outer filter hole;
The stirring hybrid chamber 4 is the cylindrical structural that intracavitary has rotary shaft 41 vertically, and its lower end is provided with discharging chamber 5.Institute State in stirring hybrid chamber 4 and be vertically arranged with rotary buffer device 42, the rotary shaft 41 is upper and lower to be vertically arranged with two groups of spiral shells respectively Vane, respectively the first helical-blade 411 and the second helical-blade 412, and the length of the second helical-blade 412 is the first helical-blade 411 1.5-2 times of length.The top of the rotary shaft 41 is provided with the first buffer subsystem 6, and the inwall 43 of the stirring hybrid chamber 4 The second buffer subsystem 61 and the 3rd buffer subsystem 62 are provided with, second buffer subsystem 61 is arranged on the first buffer subsystem 6 and the first spiral Between leaf 411, the 3rd buffer subsystem 62 is arranged between the first helical-blade 411 and the second helical-blade 412;First buffering The angle in net 6 and straight up direction is in 30-60 degree;The buffer subsystem 62 of second buffer subsystem 61 and the 3rd and vertically downward direction Angle in 30-60 degree;
Hole is set on first buffer subsystem 6, the second buffer subsystem 61 and the 3rd buffer subsystem 62.Second helical-blade 412 length is 1.5-1.8 times of the length of the first helical-blade 411.4 buffer boards are provided with the gradient hybrid chamber 2, from Up to lower is respectively the first buffer board 211, the second buffer board 212, the 3rd buffer board 213 and the 4th buffer board 214.First buffering The first filter bores, the second mistake are respectively arranged with plate 211, the second buffer board 212, the 3rd buffer board 213 and the 4th buffer board 214 Filter opening, the 3rd filter bores and the 4th filter bores.First filter bores, the second filter bores, the 3rd filter bores and the 4th filter bores Aperture ratio be 1.5:1.3:1.2:1.
In the utility model, the filter bores or hole are circle.
The utility model is further described below by specific embodiment.
Embodiment 1:A kind of plastic raw materials high efficient mixer, for mixing plastic raw materials, according to entering for plastic raw materials Material process, sequentially passes through charging aperture 1, gradient hybrid chamber 2, air blast hybrid chamber 3, stirring hybrid chamber 4 and discharging chamber 5,
The gradient hybrid chamber 2 is that into 30 ° of cylinder chamber, 4 and ground are disposed with from top to bottom inside it with ground Filter bores is of different sizes in setting filter bores 211 on the parallel buffer board 21 in face, the buffer board 21, and different buffer boards; The discharge outlet of the gradient hybrid chamber 2 is identical with the charging aperture of air blast hybrid chamber 3;
The air blast hybrid chamber 3 is that bottom is provided with the column construction of air-blast device 31, and the air blast hybrid chamber 3 is interior Intracavitary is provided with the Baltimore groove 32 of rotation, and the Baltimore groove has double-deck spill piece, and respectively outer layer spill piece 321 and internal layer is recessed Outer filter hole 3211 and internal layer mistake are respectively arranged with shape piece 322, and the outer layer spill piece 321 and internal layer spill piece 322 Filter opening, and 1.1 times of a diameter of internal layer filtering bore dia in outer filter hole;
The stirring hybrid chamber 4 is the cylindrical structural that intracavitary has rotary shaft 41 vertically, and its lower end is provided with discharging chamber 5.Institute State in stirring hybrid chamber 4 and be vertically arranged with rotary buffer device 42, the rotary shaft 41 is upper and lower to be vertically arranged with two groups of spiral shells respectively Vane, respectively the first helical-blade 411 and the second helical-blade 412, and the length of the second helical-blade 412 is the first helical-blade 411 1.5-2 times of length.The top of the rotary shaft 41 is provided with the first buffer subsystem 6, and the inwall 43 of the stirring hybrid chamber 4 The second buffer subsystem 61 and the 3rd buffer subsystem 62 are provided with, second buffer subsystem 61 is arranged on the first buffer subsystem 6 and the first spiral Between leaf 411, the 3rd buffer subsystem 62 is arranged between the first helical-blade 411 and the second helical-blade 412;First buffering The angle in net 6 and straight up direction is at 30 degree;The buffer subsystem 62 of second buffer subsystem 61 and the 3rd and vertically downward direction Angle is at 30 degree;
Hole is set on first buffer subsystem 6, the second buffer subsystem 61 and the 3rd buffer subsystem 62.Second helical-blade 412 length is 1.5 times of the length of the first helical-blade 411.4 buffer boards are provided with the gradient hybrid chamber 2, from up to It is respectively the first buffer board 211, the second buffer board 212, the 3rd buffer board 213 and the 4th buffer board 214 down.First buffer board 211st, the first filter bores, the second filtering are respectively arranged with the second buffer board 212, the 3rd buffer board 213 and the 4th buffer board 214 Hole, the 3rd filter bores and the 4th filter bores.First filter bores, the second filter bores, the 3rd filter bores and the 4th filter bores Aperture ratio is 1.5:1.3:1.2:1.
Embodiment 2:A kind of plastic raw materials high efficient mixer, for mixing plastic raw materials, according to entering for plastic raw materials Material process, sequentially passes through charging aperture 1, gradient hybrid chamber 2, air blast hybrid chamber 3, stirring hybrid chamber 4 and discharging chamber 5,
The gradient hybrid chamber 2 is that into 25-45 ° of cylinder chamber, 3-6 are disposed with from top to bottom inside it with ground The size of filter bores in filter bores 211, and different buffer boards is set on buffer board 21 parallel to the ground, the buffer board 21 It is different;The discharge outlet of the gradient hybrid chamber 2 is identical with the charging aperture of air blast hybrid chamber 3;
The air blast hybrid chamber 3 is that bottom is provided with the column construction of air-blast device 31, and the air blast hybrid chamber 3 is interior Intracavitary is provided with the Baltimore groove 32 of rotation, and the Baltimore groove has double-deck spill piece, and respectively outer layer spill piece 321 and internal layer is recessed Outer filter hole 3211 and internal layer mistake are respectively arranged with shape piece 322, and the outer layer spill piece 321 and internal layer spill piece 322 Filter opening, and 1.3 times of a diameter of internal layer filtering bore dia in outer filter hole;
The stirring hybrid chamber 4 is the cylindrical structural that intracavitary has rotary shaft 41 vertically, and its lower end is provided with discharging chamber 5.Institute State in stirring hybrid chamber 4 and be vertically arranged with rotary buffer device 42, the rotary shaft 41 is upper and lower to be vertically arranged with two groups of spiral shells respectively Vane, respectively the first helical-blade 411 and the second helical-blade 412, and the length of the second helical-blade 412 is the first helical-blade 411 2 times of length.The top of the rotary shaft 41 is provided with the first buffer subsystem 6, and the inwall 43 of the stirring hybrid chamber 4 and set There are the second buffer subsystem 61 and the 3rd buffer subsystem 62, second buffer subsystem 61 is arranged on the first buffer subsystem 6 and the first helical-blade 411 Between, the 3rd buffer subsystem 62 is arranged between the first helical-blade 411 and the second helical-blade 412;First buffer subsystem 6 with The angle in direction is at 60 degree straight up;The buffer subsystem 62 of second buffer subsystem 61 and the 3rd and the angle of vertically downward direction exist 60 degree;
Hole is set on first buffer subsystem 6, the second buffer subsystem 61 and the 3rd buffer subsystem 62.Second helical-blade 412 length is 1.8 times of the length of the first helical-blade 411.4 buffer boards are provided with the gradient hybrid chamber 2, from up to It is respectively the first buffer board 211, the second buffer board 212, the 3rd buffer board 213 and the 4th buffer board 214 down.First buffer board 211st, the first filter bores, the second filtering are respectively arranged with the second buffer board 212, the 3rd buffer board 213 and the 4th buffer board 214 Hole, the 3rd filter bores and the 4th filter bores.First filter bores, the second filter bores, the 3rd filter bores and the 4th filter bores Aperture ratio is 1.5:1.3:1.2:1.
Embodiment 3:A kind of plastic raw materials high efficient mixer, for mixing plastic raw materials, according to entering for plastic raw materials Material process, sequentially passes through charging aperture 1, gradient hybrid chamber 2, air blast hybrid chamber 3, stirring hybrid chamber 4 and discharging chamber 5,
The gradient hybrid chamber 2 is that into 30 ° of cylinder chamber, 5 and ground are disposed with from top to bottom inside it with ground Filter bores is of different sizes in setting filter bores 211 on the parallel buffer board 21 in face, the buffer board 21, and different buffer boards; The discharge outlet of the gradient hybrid chamber 2 is identical with the charging aperture of air blast hybrid chamber 3;
The air blast hybrid chamber 3 is that bottom is provided with the column construction of air-blast device 31, and the air blast hybrid chamber 3 is interior Intracavitary is provided with the Baltimore groove 32 of rotation, and the Baltimore groove has double-deck spill piece, and respectively outer layer spill piece 321 and internal layer is recessed Outer filter hole 3211 and internal layer mistake are respectively arranged with shape piece 322, and the outer layer spill piece 321 and internal layer spill piece 322 Filter opening, and 1.2 times of a diameter of internal layer filtering bore dia in outer filter hole;
The stirring hybrid chamber 4 is the cylindrical structural that intracavitary has rotary shaft 41 vertically, and its lower end is provided with discharging chamber 5.Institute State in stirring hybrid chamber 4 and be vertically arranged with rotary buffer device 42, the rotary shaft 41 is upper and lower to be vertically arranged with two groups of spiral shells respectively Vane, respectively the first helical-blade 411 and the second helical-blade 412, and the length of the second helical-blade 412 is the first helical-blade 411 1.7 times of length.The top of the rotary shaft 41 is provided with the first buffer subsystem 6, and the inwall 43 of the stirring hybrid chamber 4 and set The second buffer subsystem 61 and the 3rd buffer subsystem 62 are equipped with, second buffer subsystem 61 is arranged on the first buffer subsystem 6 and the first helical-blade Between 411, the 3rd buffer subsystem 62 is arranged between the first helical-blade 411 and the second helical-blade 412;First buffer subsystem 6 with the angle in direction straight up at 35 degree;The buffer subsystem 62 of second buffer subsystem 61 and the 3rd and the folder of vertically downward direction Angle is at 45 degree;
Hole is set on first buffer subsystem 6, the second buffer subsystem 61 and the 3rd buffer subsystem 62.Second helical-blade 412 length is 1.6 times of the length of the first helical-blade 411.4 buffer boards are provided with the gradient hybrid chamber 2, from up to It is respectively the first buffer board 211, the second buffer board 212, the 3rd buffer board 213 and the 4th buffer board 214 down.First buffer board 211st, the first filter bores, the second filtering are respectively arranged with the second buffer board 212, the 3rd buffer board 213 and the 4th buffer board 214 Hole, the 3rd filter bores and the 4th filter bores.First filter bores, the second filter bores, the 3rd filter bores and the 4th filter bores Aperture ratio is 1.5:1.3:1.2:1.

Claims (10)

1. a kind of plastic raw materials high efficient mixer, for mixing plastic raw materials, it is characterised in that according to entering for plastic raw materials Material process, sequentially passes through charging aperture, gradient hybrid chamber, air blast hybrid chamber, stirring hybrid chamber and discharging chamber,
The gradient hybrid chamber is that into 25-45 ° of cylinder chamber, 3-6 and ground are disposed with from top to bottom inside it with ground Filter bores are set on the parallel buffer board in face, the buffer board, and on different buffer boards filter bores it is of different sizes;The gradient The discharge outlet of hybrid chamber is identical with the charging aperture of air blast hybrid chamber;
The air blast hybrid chamber is provided with the column construction of air-blast device for bottom, and the interior intracavitary of the air blast hybrid chamber is set There is the Baltimore groove of rotation, the Baltimore groove has double-deck spill piece, respectively outer layer spill piece and internal layer spill piece, and described outer Be respectively arranged with outer filter hole and internal layer filter bores on layer spill piece and internal layer spill piece, and outer filter hole it is a diameter of in 1.1-1.3 times of layer filtering bore dia;
The stirring hybrid chamber is the cylindrical structural that intracavitary has rotary shaft vertically, and its lower end is provided with discharging chamber.
2. plastic raw materials high efficient mixer as claimed in claim 1, it is characterised in that be vertically arranged with rotation in stirring hybrid chamber Turn buffer unit, the rotary shaft is upper and lower to be vertically arranged with two groups of helical-blades, respectively the first helical-blade and the second spiral respectively Leaf, and the length of the second helical-blade is 1.5-2 times of the first helical-blade length.
3. plastic raw materials high efficient mixer as claimed in claim 1, it is characterised in that is provided with the top of the rotary shaft The second buffer subsystem and the 3rd buffer subsystem, second buffer subsystem are provided with one buffer subsystem, and the inwall of the stirring hybrid chamber Be arranged between the first buffer subsystem and the first helical-blade, the 3rd buffer subsystem be arranged on the first helical-blade and the second helical-blade it Between;
The angle in first buffer subsystem and straight up direction is in 30-60 degree;
Second buffer subsystem and the 3rd buffer subsystem and the angle of vertically downward direction are in 30-60 degree;
Hole is set on first buffer subsystem, the second buffer subsystem and the 3rd buffer subsystem.
4. the plastic raw materials high efficient mixer described in claim 2, it is characterised in that the length of second helical-blade is first 1.5-1.8 times of helical-blade length.
5. the plastic raw materials high efficient mixer described in claim 1, it is characterised in that be provided with 4 in the gradient hybrid chamber Individual buffer board, from top to bottom respectively the first buffer board, the second buffer board, the 3rd buffer board and the 4th buffer board.
6. the plastic raw materials high efficient mixer described in claim 4, it is characterised in that the first buffer board, the second buffer board, the 3rd The first filter bores, the second filter bores, the 3rd filter bores and the 4th filter bores are respectively arranged with buffer board and the 4th buffer board.
7. the plastic raw materials high efficient mixer described in claim 6, it is characterised in that first filter bores, the second filter bores, The aperture ratio of 3rd filter bores and the 4th filter bores is 1.5:1.3:1.2:1.
8. the plastic raw materials high efficient mixer described in claim 3, it is characterised in that first buffer subsystem and side straight up To angle at 50 degree.
9. the plastic raw materials high efficient mixer described in claim 3, it is characterised in that second buffer subsystem and side straight down To angle at 45 degree.
10. the plastic raw materials high efficient mixer described in claim 3, it is characterised in that the 3rd buffer subsystem with straight down The angle in direction is at 35 degree.
CN201720134999.8U 2017-02-15 2017-02-15 A kind of plastic raw materials high efficient mixer Expired - Fee Related CN206493471U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109228229A (en) * 2018-08-14 2019-01-18 海宁市现代五金有限公司 A kind of processing technology of high light transmission lampshade

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109228229A (en) * 2018-08-14 2019-01-18 海宁市现代五金有限公司 A kind of processing technology of high light transmission lampshade
CN109228229B (en) * 2018-08-14 2023-10-13 海宁市现代五金有限公司 Processing technology of high-light-transmission lampshade

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