CN111744421A - Continuous feeding mixer - Google Patents
Continuous feeding mixer Download PDFInfo
- Publication number
- CN111744421A CN111744421A CN202010707266.5A CN202010707266A CN111744421A CN 111744421 A CN111744421 A CN 111744421A CN 202010707266 A CN202010707266 A CN 202010707266A CN 111744421 A CN111744421 A CN 111744421A
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- Prior art keywords
- mixer
- side wall
- material distribution
- shell
- distribution pipe
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
- B01F33/811—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles in two or more consecutive, i.e. successive, mixing receptacles or being consecutively arranged
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
Abstract
The invention provides a continuous feeding mixer, which comprises at least 2 material mixers connected in series; the material mixer comprises a shell with two closed ends, a material distribution pipe arranged at one end of the shell, a side wall feed inlet arranged on the side wall of the shell and close to one side of the material distribution pipe, a discharge outlet arranged on the side wall of the shell and far away from the material distribution pipe, and a filler arranged in the shell and positioned between the tail end of the material distribution pipe and the discharge outlet; along the material flow direction, the discharge port of the material mixer of the previous stage is connected with the side wall feed port of the adjacent material mixer; the continuous feeding mixer can not only mix a plurality of reaction materials step by step, but also ensure the mixing effect of each material.
Description
Technical Field
The invention belongs to the technical field of continuous reaction, relates to a mixer, and particularly relates to a continuous feeding mixer.
Background
The materials react in the kettle type reactor, mechanical stirring is required to be continuously carried out in the reaction process, but the energy consumption of the mechanical stirring is higher, and the premixing is carried out before the materials enter the reaction kettle, so that the requirement on the mechanical stirring can be reduced, and the conversion rate in the reaction process can be improved.
In the premixing process, if a plurality of materials are directly mixed, the defect of more byproducts caused by the reaction sequence of the plurality of materials cannot be overcome; if simple carry out two liang of mixings with multiple material, then be unfavorable for saving the mix time, also be unfavorable for improving the mixture homogeneity of multiple material.
CN 205288173U discloses continuous compounding device of living beings raw materials, including storing groove, conveyer pipe, delivery pump, feeder hopper, leak protection groove, compounding groove, agitator motor, (mixing) shaft, compounding scraper group and discharge gate, the (mixing) shaft level sets up in the compounding inslot, install a plurality of groups compounding scraper group on the (mixing) shaft, compounding scraper group is including forward scraper, reverse scraper and fixed strut. The mixing device can continuously mix materials, is reasonable in structure and simple to operate, and has the defect of generating more byproducts for a multi-material system with a reaction sequence.
CN 209222079U discloses a liquid-liquid continuous reaction device, which has a main body of the reaction device, the main body of the continuous reaction device includes a pipeline, a left flange head and a right flange head, the liquid-liquid reaction device also has a reactant outlet on the right flange head, the liquid-liquid reaction device has a heat exchange medium inlet and a heat exchange medium outlet on the pipeline of the main body of the reaction device, the liquid-liquid continuous reaction device also has a plurality of upper baffles, a plurality of lower baffles and a plurality of material inlets, the baffles divide the main body of the reaction device into at least two reaction sections, and the bed charge reacts with the materials from different material inlets in different reaction sections step by step. However, the mixing of a plurality of materials in the liquid-liquid continuous reaction device requires a large space and the mixing effect is poor.
Therefore, there is a need for a simple continuous feed mixer that can be used for step-wise mixing of multiple materials.
Disclosure of Invention
Aiming at the defects in the prior art, the invention aims to provide a continuous feed mixer. The continuous feeding mixer is simple in structure, can uniformly mix more than 3 materials, and can mix a plurality of materials step by step, so that the generation of reaction byproducts is reduced, and the conversion rate of the reaction is improved.
In order to achieve the purpose, the invention adopts the following technical scheme:
the invention provides a continuous feed mixer, which comprises at least 2 material mixers connected in series.
The material mixer comprises a shell with two closed ends, a material distribution pipe arranged at one end of the shell, a side wall feed inlet arranged on the side wall of the shell and close to one side of the material distribution pipe, a discharge outlet arranged on the side wall of the shell and far away from the material distribution pipe, and a filler arranged in the shell and positioned between the tail end of the material distribution pipe and the discharge outlet;
along the material flowing direction, the discharge port of the material mixer of the previous stage is connected with the side wall feed port of the adjacent material mixer.
The continuous feed mixer according to the invention comprises at least 2 material mixers connected in series, for example 2, 3, 4, 5, 6, 7, 8 or 10, but is not limited to the values listed, and other values not listed in the numerical range are equally applicable.
Illustratively, when 3 materials need to be mixed, the continuous feed mixer includes 2 material mixers connected in series; when 4 materials need to be mixed, the continuous feeding mixer comprises 3 material mixers connected in series; when 5 materials need to be mixed, the continuous feeding mixer comprises 2 material mixers connected in series; namely, when n materials need to be mixed, the continuous feeding mixer comprises n-1 material mixers connected in series, wherein n is a positive integer more than or equal to 3.
The continuous feeding mixer is a continuous feeding mixer for mixing liquid-phase materials and/or gas-phase materials, taking 3 materials as an example, the continuous feeding mixer comprises 2 material mixers connected in series, wherein a material 1 is fed from a side wall feed inlet of a 1 st-stage material mixer, a material 2 is fed from a material distribution pipe of the 1 st-stage material mixer, the material 1 and the material 2 are mixed in the 1 st-stage material mixer, flow through a filler, flow into the side wall feed inlet of the 2 nd-stage material mixer from a discharge port, are mixed with a material 3 flowing out from the material distribution pipe of the 2 nd-stage material mixer, flow through the filler, and are discharged from the discharge port of the 2 nd-stage material mixer, so that the mixing of the material 1, the material 2 and the material 3 is completed.
Preferably, in the material mixer, the material distribution pipe is coincident with the central axis of the shell.
Preferably, the side wall of the material distribution pipe close to the filling end is provided with material distribution holes.
According to the invention, the material distribution pipe is overlapped with the central axis of the shell, and the side wall of the material distribution pipe is provided with the material distribution holes, so that the material flowing out of the material distribution pipe can be uniformly distributed in the radial direction of the material distribution pipe, and the material mixing effect is further improved.
The material distribution pipe of the present invention is preferably a material distribution pipe with a regular shape, such as a circular pipe or a square pipe. The material distribution holes are preferably regular-shaped material distribution holes, such as circular holes, square holes or strip-shaped holes.
Preferably, the material distribution holes are of equal diameter. The equal diameters are equal diameters of equivalent circles of the material distribution holes, and the equal diameters of the material distribution holes comprise equal diameters of the material distribution holes on the same material distribution pipe, or equal diameters of the material distribution holes on all the material distribution pipes of the continuous feed mixer, preferably equal diameters of the material distribution holes on all the material distribution pipes of the continuous feed mixer.
It is further preferred that the diameter of the material distribution holes is 1-8mm, for example 1mm, 2mm, 3mm, 4mm, 5mm, 6mm, 7mm or 8mm, but not limited to the values recited, and other values not recited within the range of values are equally applicable; the diameter is the equivalent circle diameter.
Preferably, the material distribution holes are arranged at equal intervals. The equidistant arrangement of the material distribution holes means that the central distances of any two adjacent material distribution holes on the same material distribution pipe are equal.
It is further preferred that the distance between the centers of any two adjacent material distribution openings on the same material distribution pipe is 5-15mm, such as 5mm, 6mm, 7mm, 8mm, 9mm, 10mm, 11mm, 12mm, 13mm, 14mm or 15mm, but not limited to the values listed, and other values not listed in the range of values are equally applicable. The center distance is the distance between the centers of any two adjacent material distribution holes along the surface connecting line of the material distribution pipes.
Preferably, the packing comprises structured packing and/or random packing.
The filler has a large specific surface area, and the mixed materials can be uniformly mixed in the filler. The structured packing includes, but is not limited to, any one or combination of at least two of 250Y structured packing, BX structured packing, or 400X structured packing, and typical but non-limiting combinations include combinations of 250Y structured packing and BX structured packing, BX structured packing and 400X structured packing, 250Y structured packing and 400X structured packing, or combinations of 250Y structured packing, BX structured packing and 400X structured packing.
The random packing comprises any one or combination of at least two of a pall ring, a step ring or an intalox ring, and typical but non-limiting combinations comprise a combination of a pall ring and a step ring, a combination of a step ring and an intalox ring, a combination of a pall ring and an intalox ring or a combination of a pall ring, a step ring and an intalox ring.
Preferably, in the material flow direction, the two sides of the filler are provided with filler compacting structures.
The packing press structure is a packing press mechanism conventional in the art for securing the packing in a fixed position within the housing. The filler compaction structure provided by the invention enables the filler to be stable under the flow field condition of high flow rate, thereby ensuring the mixing effect of fluid in the filler and enabling various materials to be fully and uniformly mixed in the continuous feeding mixer.
Preferably, along the material flowing direction, the connection mode of the discharge port of the material mixer of the previous stage and the side wall feed port of the adjacent material mixer comprises welding connection and/or flange connection; further preferred is a flange connection.
The flange connection structure is convenient for the detachable connection of two adjacent material mixers, so that the material mixers can be detached and assembled according to different quantities of mixed materials.
Preferably, the material mixer comprises an end discharge port or a side wall discharge port.
Preferably, the end discharge port is a concentric reducing pipe, and a large-diameter end of the concentric reducing pipe is connected with the end of the shell.
The concentric reducer is used for improving the flow velocity by changing the flow area of the pipeline so as to accelerate the flow velocity of the fluid and lead solid particles possibly existing in the material to be brought out of the continuous feeding mixer by the fluid, thereby avoiding the aggregation and sedimentation of the solid particles possibly existing at the rear part of the filler and avoiding the risk of filler blockage.
Moreover, the arrangement of the concentric reducing pipes can reduce local resistance; furthermore, the end discharge hole and the side wall feed inlet are connected through the elbow in a flange mode, local resistance can be further reduced, pressure drop can be reduced due to the fact that the local resistance is reduced, and therefore the effect of saving energy consumption is achieved.
The continuous feed mixer provided by the invention can be used for mixed feed of multi-material chemical reaction, and the application comprises the following steps: any two materials in the multiple materials are mixed to obtain a mixed material, and then the mixed material and the rest materials are sequentially mixed.
The "multi-material" in the invention refers to more than three materials.
The invention discloses that the mixed materials are sequentially mixed with the rest materials, and the two materials are firstly mixed, then mixed with the third material, mixed with the fourth material and the like. Exemplary, the continuous feed mixer of the first aspect is used for four material chemical reaction applications: firstly, mixing any two of the four materials to obtain a first mixed material; then mixing the first mixed material with any one of the rest two materials to obtain a second mixed material; and finally, mixing the second mixed material with the last material to perform chemical reaction.
Compared with the prior art, the invention has the beneficial effects that:
(1) according to the invention, at least 2 material mixers connected in series can be used for uniformly mixing more than 3 gas-phase materials and/or liquid-phase materials, mixing can be carried out according to the sequence of material reaction, meanwhile, the full mixing of various materials can be ensured, the effective conversion rate of the reaction is improved, and the energy consumption is saved;
(2) according to the invention, two adjacent material mixers are detachably connected, so that the continuous feeding mixer can be flexibly adjusted according to the quantity of mixed materials, and the continuous feeding mixer is suitable for different places and working environments;
(3) the filler compaction structure ensures that the filler can be stable under the flow field condition of high flow rate, thereby ensuring the mixing effect of fluid in the filler and fully and uniformly mixing various materials in a continuous feeding mixer;
(4) the invention changes the flow area of the pipeline by the arrangement of the concentric reducing pipes, thereby realizing the purpose of improving the flow speed of the tail end, leading possible solid particles in the material to be brought out of the continuous feeding mixer by fluid, avoiding the possible aggregation and sedimentation of the solid particles at the rear part of the filler and avoiding the risk of filler blockage; the arrangement of the concentric reducing pipes can reduce local resistance, and the reduction of the local resistance can lead to the reduction of pressure drop, thereby achieving the effect of saving energy consumption.
Drawings
FIG. 1 is a schematic structural view of a continuous feed mixer provided in example 1;
FIG. 2 is a schematic structural view of a continuous feed mixer provided in example 2;
fig. 3 is a schematic structural diagram of a continuous feed mixer provided in example 3.
Wherein: 1, a shell; 2, a material distribution pipe; 2-1, material distribution holes; 3, a side wall feed inlet; 4, discharging a material outlet; 5, filling; 6, a packing compaction structure; and 7, concentric reducing pipes.
Detailed Description
It is to be understood that in the description of the present invention, the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc., indicate orientations or positional relationships based on those shown in the drawings, and are used only for convenience in describing the present invention and for simplicity in description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be taken as limiting the present invention.
It should be noted that, in the description of the present invention, unless otherwise explicitly specified or limited, the terms "disposed," "connected" and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood by those of ordinary skill in the art through specific situations.
The technical scheme of the invention is further explained by the specific implementation mode in combination with the attached drawings.
As a preferable technical solution of the continuous feed mixer of the present invention, the continuous feed mixer includes at least 2 material mixers connected in series; the material mixer comprises a shell 1 with two closed ends, a material distribution pipe 2 arranged at one end of the shell 1, a side wall feed inlet 3 arranged on the side wall of the shell 1 and close to one side of the material distribution pipe 2, a discharge outlet 4 arranged on the side wall of the shell 1 and far away from the material distribution pipe 2, and a filler 5 arranged in the shell 1 and positioned between the tail end of the material distribution pipe 2 and the discharge outlet 4; along the material flow direction, the discharge port 4 of the material mixer of the previous stage is detachably connected with the side wall feed port 3 of the adjacent material mixer through a flange.
In the material mixer, a material distribution pipe 2 is superposed with the central axis of a shell 1; the side wall of the material distribution pipe 2 close to the end of the filler 5 is provided with a plurality of material distribution holes 2-1 with equal diameters, and the center distances of any adjacent 2 material distribution holes 2-1 are equal.
The packing 5 comprises structured packing and/or random packing; and a packing compacting structure 6 is arranged on two sides of the packing 5 along the material flowing direction.
The material outlet 4 of the material mixer comprises an end outlet or a side wall outlet, the end outlet is preferably a concentric reducing pipe 7, and the large end of the concentric reducing pipe 7 is connected with the end of the shell 1.
For space limitation, the embodiment of the present invention is exemplified by a continuous feed mixer for mixing 3 materials, and the continuous feed mixer for mixing 3 materials comprises 2 material mixers connected in series.
Example 1
The present example provides a continuous feed mixer as shown in fig. 1, comprising 2 material mixers connected in series; the material mixer comprises a shell 1 with two closed ends, a circular material distribution pipe 2 arranged at one end of the shell 1, a side wall feed inlet 3 arranged on the side wall of the shell 1 and close to one side of the circular material distribution pipe 2, a discharge outlet 4 arranged on the side wall of the shell 1 and far away from the circular material distribution pipe 2, and a filler 5 arranged in the shell 1 and positioned between the tail end of the circular material distribution pipe 2 and the discharge outlet 4; along the material flow direction, the end discharge port of the 1 st-stage material mixer is detachably connected with the side wall feed inlet 3 of the 2 nd-stage material mixer through a flange.
In the material mixer, a circular material distribution pipe 2 is superposed with the central axis of a shell 1; the side wall of the circular material distribution pipe 2 close to the end of the filler 5 is provided with a plurality of circular material distribution holes 2-1 with the equivalent circle diameter of 3mm, and the center distance of any adjacent 2 material distribution holes 2-1 is 10 mm.
The packing 5 is a 250Y structured packing; and a packing compacting structure 6 is arranged on two sides of the packing 5 along the material flowing direction.
The discharge port 4 of the 2 nd-stage material mixer is an end discharge port, the end discharge port is a concentric reducing pipe 7, and the large-diameter end of the concentric reducing pipe 7 is connected with the end part of the shell 1.
When the continuous feeding mixer provided by the embodiment is used for mixing materials, a first material is fed from a side wall feed port 3 of a 1 st-level material mixer, a second material is fed from a material distribution pipe 2 of the 1 st-level material mixer, the first material and the second material are mixed in the 1 st-level material mixer and flow through a filler 5, then flow into the side wall feed port 3 of the 2 nd-level material mixer from an end discharge port 4, and are mixed with a third material flowing out from the material distribution pipe 2 of the 2 nd-level material mixer, and after flowing through the filler 5, the third material is discharged from an end discharge port of the 2 nd-level material mixer, so that the mixing of the first material, the second material and the third material is completed.
Example 2
The present embodiment provides a continuous feed mixer as shown in fig. 2, comprising 2 material mixers connected in series; the material mixer comprises a shell 1 with two closed ends, a square material distribution pipe 2 arranged at one end of the shell 1, a side wall feed inlet 3 arranged on the side wall of the shell 1 and close to one side of the square material distribution pipe 2, a discharge outlet 4 arranged on the side wall of the shell 1 and far away from the square material distribution pipe 2, and a filler 5 arranged in the shell 1 and positioned between the tail end of the square material distribution pipe 2 and the discharge outlet 4; along the material flow direction, the side wall discharge port of the 1 st-stage material mixer is detachably connected with the side wall feed port 3 of the 2 nd-stage material mixer through a flange.
In the material mixer, a square material distribution pipe 2 is superposed with the central axis of a shell 1; the side wall of the square material distribution pipe 2 close to the end of the filler 5 is provided with a plurality of square material distribution holes 2-1 with the equivalent circle diameter of 8mm, and the center distance of any adjacent 2 material distribution holes 2-1 is 15 mm.
The filler 5 is a random packing consisting of a pall ring, a stepped ring and a rectangular saddle ring; and a packing compacting structure 6 is arranged on two sides of the packing 5 along the material flowing direction.
The discharge port 4 of the 1 st-stage material mixer is a side wall discharge port, the discharge port 4 of the 2 nd-stage material mixer is an end discharge port, the end discharge port is a concentric reducing pipe 7, and the large-diameter end of the concentric reducing pipe 7 is connected with the end of the shell 1.
When the continuous feeding mixer provided by the embodiment is used for mixing materials, a first material is fed from the side wall feed port 3 of the 1 st-level material mixer, a second material is fed from the material distribution pipe 2 of the 1 st-level material mixer, the first material and the second material are mixed in the 1 st-level material mixer and flow through the filler 5, then flow into the side wall feed port 3 of the 2 nd-level material mixer from the side wall discharge port 4, and are mixed with a third material flowing out from the material distribution pipe 2 of the 2 nd-level material mixer, and after flowing through the filler 5, the third material is discharged from the discharge port 4 of the 2 nd-level material mixer, so that the mixing of the first material, the second material and the third material is completed.
Example 3
The present embodiment provides a continuous feed mixer as shown in fig. 3, comprising 2 material mixers connected in series; the material mixer comprises a shell 1 with two closed ends, a circular material distribution pipe 2 arranged at one end of the shell 1, a side wall feed inlet 3 arranged on the side wall of the shell 1 and close to one side of the circular material distribution pipe 2, a discharge outlet 4 arranged on the side wall of the shell 1 and far away from the circular material distribution pipe 2, and a filler 5 arranged in the shell 1 and positioned between the tail end of the circular material distribution pipe 2 and the discharge outlet 4; along the material flow direction, the end discharge port of the 1 st-stage material mixer is detachably connected with the side wall feed inlet 3 of the 2 nd-stage material mixer through a flange.
In the material mixer, a circular material distribution pipe 2 is superposed with the central axis of a shell 1; the side wall of the circular material distribution pipe 2 close to the end of the filler 5 is provided with a plurality of strip-shaped material distribution holes 2-1 with the equivalent circle diameter of 1mm, and the center distance of any adjacent 2 material distribution holes 2-1 is 5 mm.
The packing 5 is a BX regular packing; and a packing compacting structure 6 is arranged on two sides of the packing 5 along the material flowing direction.
The discharge port 4 of the 1 st-stage material mixer is an end discharge port, and the discharge port 4 of the 2 nd-stage material mixer is an end discharge port; the tip discharge gate is concentric reducing pipe 7, and the end connection of the big footpath end and the casing 1 of concentric reducing pipe 7, and the detachable connection is realized through elbow and 2 grade material mixer's lateral wall feed inlet 3 to the tip discharge gate of 1 grade material mixer.
When the continuous feeding mixer provided by the embodiment is used for mixing materials, a first material is fed from the side wall feed port 3 of the 1 st-level material mixer, a second material is fed from the material distribution pipe 2 of the 1 st-level material mixer, the first material and the second material are mixed in the 1 st-level material mixer and flow through the filler 5, then flow into the side wall feed port 3 of the 2 nd-level material mixer from the end discharge port and are mixed with a third material flowing out from the material distribution pipe 2 of the 2 nd-level material mixer, and after flowing through the filler 5, the third material is discharged from the end discharge port of the 2 nd-level material mixer, so that the mixing of the first material, the second material and the third material is completed.
The continuous feeding mixer provided by the embodiments 1-3 of the present invention can be applied to the chemical reaction of multiple materials, and compared with the conventional feeding mode, the continuous feeding mixer provided by the present invention can realize the distributed feeding and the sufficient mixing of multiple materials, thereby reducing the energy consumption and improving the conversion rate of the chemical reaction.
In conclusion, the invention can uniformly mix more than 3 gas-phase materials and/or liquid-phase materials through at least 2 material mixers connected in series, can mix materials according to the sequence of material reaction, and can ensure the mixing effect of various materials; according to the invention, two adjacent material mixers are detachably connected, so that the continuous feeding mixer can be flexibly adjusted according to the quantity of mixed materials, and the continuous feeding mixer is suitable for different places and working environments; the filler compaction structure ensures that the filler can be stable under the flow field condition of high flow rate, thereby ensuring the mixing effect of fluid in the filler and uniformly mixing various materials in the continuously fed mixed gas; the invention changes the flow area of the pipeline by the arrangement of the concentric reducing pipes, thereby realizing the purpose of improving the flow speed of the tail end, leading possible solid particles in the material to be carried out of the continuous feeding mixer by fluid, avoiding the possible aggregation and sedimentation of the solid particles at the rear part of the filler and avoiding the risk of filler blockage.
The applicant declares that the above description is only a specific embodiment of the present invention, but the scope of the present invention is not limited thereto, and it should be understood by those skilled in the art that any changes or substitutions that can be easily conceived by those skilled in the art within the technical scope of the present invention are within the scope and disclosure of the present invention.
Claims (10)
1. A continuous feed mixer, characterized in that the continuous feed mixer comprises at least 2 material mixers connected in series;
the material mixer comprises a shell with two closed ends, a material distribution pipe arranged at one end of the shell, a side wall feed inlet arranged on the side wall of the shell and close to one side of the material distribution pipe, a discharge outlet arranged on the side wall of the shell and far away from the material distribution pipe, and a filler arranged in the shell and positioned between the tail end of the material distribution pipe and the discharge outlet;
along the material flowing direction, the discharge port of the material mixer of the previous stage is connected with the side wall feed port of the adjacent material mixer.
2. A continuous feed mixer according to claim 1 wherein the material distribution pipe coincides with the central axis of the housing.
3. A continuous feed mixer according to claim 1 or 2, wherein the side wall of the material distribution pipe near the filler end is provided with material distribution holes.
4. A continuous feed mixer according to claim 3 wherein the material distribution apertures are of equal diameter.
5. A continuous feed mixer according to claim 4 wherein the material distribution apertures are equally spaced.
6. The continuous feed mixer of claim 1, wherein the packing comprises structured packing and/or random packing.
7. A continuous feed mixer according to claim 6, wherein the packing is provided with packing constrictions on both sides in the direction of flow of the material.
8. The continuous feed mixer of claim 1, wherein the connection of the discharge port of the material mixer of the previous stage to the side wall feed port of the adjacent material mixer in the material flow direction comprises a welded connection and/or a flanged connection.
9. The continuous feed mixer of claim 1, wherein the material mixer discharge comprises an end discharge or a side wall discharge.
10. The continuous feed mixer of claim 9, wherein the end discharge port is a concentric reducer having a large diameter end coupled to the end of the housing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010707266.5A CN111744421A (en) | 2020-07-21 | 2020-07-21 | Continuous feeding mixer |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010707266.5A CN111744421A (en) | 2020-07-21 | 2020-07-21 | Continuous feeding mixer |
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| CN111744421A true CN111744421A (en) | 2020-10-09 |
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| CN202010707266.5A Pending CN111744421A (en) | 2020-07-21 | 2020-07-21 | Continuous feeding mixer |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112221406A (en) * | 2020-12-09 | 2021-01-15 | 佛山市普力达科技有限公司 | Full-grade silicone adhesive continuous production system |
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2020
- 2020-07-21 CN CN202010707266.5A patent/CN111744421A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112221406A (en) * | 2020-12-09 | 2021-01-15 | 佛山市普力达科技有限公司 | Full-grade silicone adhesive continuous production system |
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