CN110756073A - Chemical liquid shunting spiral hedging mixer - Google Patents
Chemical liquid shunting spiral hedging mixer Download PDFInfo
- Publication number
- CN110756073A CN110756073A CN201911222251.3A CN201911222251A CN110756073A CN 110756073 A CN110756073 A CN 110756073A CN 201911222251 A CN201911222251 A CN 201911222251A CN 110756073 A CN110756073 A CN 110756073A
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- CN
- China
- Prior art keywords
- pipe
- spiral
- hedging
- opposite
- chemical liquid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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Classifications
-
- 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
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
-
- 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
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
- B01F25/4314—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles
-
- 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
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
- B01F25/4316—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being flat pieces of material, e.g. intermeshing, fixed to the wall or fixed on a central rod
-
- 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
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/432—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
-
- 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
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
-
- 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
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
- B01F25/4331—Mixers with bended, curved, coiled, wounded mixing tubes or comprising elements for bending the flow
Abstract
The invention discloses a chemical liquid diversion spiral hedging mixer, which comprises a material diversion pipe, a plurality of diversion pipes, a spiral hedging mixing pipe and a finished discharge pipe which are sequentially connected, and is characterized in that: the material flow dividing pipe comprises a main pipe and a plurality of branch pipes; the end parts of the branch pipes are connected with a flow guide pipe, and the other end of the flow guide pipe is connected with the left end or the right end of the spiral opposite-flushing mixing pipe; both ends of the spiral opposite-impact mixing pipe are connected with at least one flow guide pipe; the middle part of the spiral opposite-flushing mixing pipe is connected with a finished product discharging pipe. The invention utilizes the material shunt tubes to divide the material into two paths, and finally realizes the self-hedging mixing of the material; a spoiler is arranged in the main pipe of the material flow dividing pipe to realize premixing of various liquid materials; through helical fin, make the material flow be the screw motion, be opposite direction rotatory striking when two strands of materials offset, it is better to mix the effect.
Description
Technical Field
The invention relates to the technical field of chemical liquid mixing, in particular to a chemical liquid shunting spiral hedging mixer.
Background
In petrochemical production, mixing of various liquid chemical raw materials is a frequently used production operation mode, and some existing liquid mixing equipment are large in size, complex in structure, high in energy consumption and required to be stirred by power; some small volume, but poor mixing effect, affects product quality.
Disclosure of Invention
The invention aims to overcome the defects in the prior art and provides the chemical liquid shunting spiral hedging mixer which is simple in structure, good in mixing effect, capable of quickly mixing various liquid materials by utilizing the pumping pressure of a production system, capable of improving the product quality and reducing the energy consumption.
The invention is realized by the following modes: the utility model provides a chemical industry liquid reposition of redundant personnel spiral is to dashing blender, includes consecutive material shunt tubes 1, a plurality of honeycomb duct 2, spiral offset mixing tube 3, becomes discharging pipe 4, its characterized in that: the material shunt pipe 1 comprises a main pipe 12 and a plurality of branch pipes 13; the end parts of the branch pipes 13 are connected with a flow guide pipe 2, and the other end of the flow guide pipe 2 is connected with the left end or the right end of the spiral opposite-flushing mixing pipe 3; both ends of the spiral opposite-impact mixing pipe 3 are at least connected with a flow guide pipe 2; the middle part of the spiral opposite-flushing mixing pipe 3 is connected with a finished product discharging pipe 4.
Further, the number of the branch pipes 13 is preferably two; the number of the draft tubes 2 is two.
Further, spoilers 11 are arranged in the main pipe 12 of the material flow dividing pipe 1 in a staggered manner; the top of the material shunt pipe 1 is provided with a material inlet 5.
Further, the honeycomb duct 2 is an arc-shaped pipeline.
Further, a spiral fin 31 is arranged in the spiral opposite-punching mixing pipe 3.
Further, the spiral fin 31 is fixed in the spiral opposite-punching mixing pipe 3; the helical fin 31 is composed of a central shaft and fins spirally wound around the central shaft in the axial direction thereof.
Further, the middle part of the spiral opposite-flushing mixing pipe 3 is vertically provided with an opening 32; the opening 32 is connected with the finished product discharge pipe 4; a material opposite-flushing mixing area is arranged right below the opening 32.
Further, the finished product discharge pipe 4 is vertically arranged upwards; and the top of the finished product discharge pipe 4 is a finished product outlet 6.
Further, the spiral opposite-impact mixing pipe 3 is horizontally arranged.
The invention has the beneficial effects that: 1. the invention utilizes the material shunt tubes to divide the material into two paths, and finally realizes the self-hedging mixing of the material;
2. according to the invention, the spoilers are arranged on the main pipe of the material flow dividing pipe, so that various liquid materials are premixed;
3. according to the invention, the material flows in a spiral motion through the spiral fins, and two materials rotate and impact in opposite directions when being collided, so that the mixing effect is better;
4. finished product discharging pipe is the design that makes progress perpendicularly, avoids because of material self gravity reason, causes the mixed effect not good, has further improved mixed effect.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings that are required to be used in the embodiments will be briefly described below, it should be understood that the following drawings only illustrate some embodiments of the present invention and therefore should not be considered as limiting the scope, and for those skilled in the art, other related drawings can be obtained according to the drawings without inventive efforts.
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a cross-sectional view of the present invention;
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention more apparent, the technical solutions of the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings of the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all embodiments of the present invention. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, are within the scope of the present invention. Thus, the following detailed description of the embodiments of the present invention, presented in the figures, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, are within the scope of the present invention.
In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "front", "rear", "both ends", "one end", "the other end", and the like indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "provided," "connected," and the like are to be construed broadly, such as "connected," which may be 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 meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
Example 1:
as shown in fig. 1-2, a chemical liquid reposition of redundant personnel spiral offset blender, including consecutive material shunt tubes 1, two honeycomb ducts 2, spiral offset mixing tube 3, become discharging pipe 4, its characterized in that: the material shunt pipe 1 comprises a main pipe 12 and two branch pipes 13; the end parts of the branch pipes 13 are connected with a flow guide pipe 2, and the other end of the flow guide pipe 2 is connected with the left end or the right end of the spiral opposite-flushing mixing pipe 3; both ends of the spiral opposite-impact mixing pipe 3 are at least connected with a flow guide pipe 2; the middle part of the spiral opposite-flushing mixing pipe 3 is connected with a finished product discharging pipe 4.
Further, spoilers 11 are arranged in the main pipe 12 of the material flow dividing pipe 1 in a staggered manner; the top of the material shunt pipe 1 is provided with a material inlet 5.
Further, the honeycomb duct 2 is an arc-shaped pipeline.
Further, a spiral fin 31 is arranged in the spiral opposite-punching mixing pipe 3.
Further, the spiral fin 31 is fixed in the spiral opposite-punching mixing pipe 3; the helical fin 31 is composed of a central shaft and fins spirally wound around the central shaft in the axial direction thereof.
Further, the middle part of the spiral opposite-flushing mixing pipe 3 is vertically provided with an opening 32; the opening 32 is connected with the finished product discharge pipe 4; a material opposite-flushing mixing area is arranged right below the opening 32.
Further, the finished product discharge pipe 4 is vertically arranged upwards; and the top of the finished product discharge pipe 4 is a finished product outlet 6.
Further, the spiral opposite-impact mixing pipe 3 is horizontally arranged.
The working principle is as follows: various materials enter the material flow dividing pipe 1 through the material inlet 5, and a spoiler 11 is arranged in a main pipe 12 of the material flow dividing pipe 1 so as to pre-mix the materials; after the materials are premixed, the materials respectively flow into the two flow guide pipes 2 from the two branch pipes 13 of the material flow guide pipe 1; after two materials come out of the two flow guide pipes 2, the two materials enter the spiral opposite-flushing mixing pipe 3 from the two ends of the spiral opposite-flushing mixing pipe 3, and because the spiral fins 31 are arranged in the spiral opposite-flushing mixing pipe 3, the two liquids form reverse spiral motion after entering from the two ends of the spiral opposite-flushing mixing pipe 3, and form reverse spiral opposite-flushing in a material opposite-flushing mixing area in the middle of the spiral opposite-flushing mixing pipe 3, so that the aim of fully mixing is fulfilled; the mixed finished product flows out from a finished product outlet 6 through a finished product discharging pipe 4 along the vertical upward direction.
The invention utilizes the material shunt tubes to divide the material into two paths, and finally realizes the self-hedging mixing of the material;
according to the invention, the spoilers are arranged on the main pipe of the material flow dividing pipe, so that various liquid materials are premixed;
according to the invention, the material flows in a spiral motion through the spiral fins, and two materials rotate and impact in opposite directions when being collided, so that the mixing effect is better;
finished product discharging pipe is the design that makes progress perpendicularly, avoids because of material self gravity reason, causes the mixed effect not good, has further improved mixed effect.
The branch pipes 13 and the draft pipes 2 can be arranged in various combinations of 4, 6, 8 and the like.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (9)
1. The utility model provides a chemical industry liquid reposition of redundant personnel spiral hedging blender, includes consecutive material shunt tubes (1), a plurality of honeycomb duct (2), spiral hedging hybrid tube (3), becomes discharging pipe (4), its characterized in that: the material shunt pipe (1) comprises a main pipe (12) and a plurality of shunt pipes (13); the end parts of the branch pipes (13) are connected with a flow guide pipe (2), and the other end of the flow guide pipe (2) is connected with the left end or the right end of the spiral opposite-flushing mixing pipe (3); both ends of the spiral opposite-impact mixing pipe (3) are connected with at least one guide pipe (2); the middle part of the spiral opposite-flushing mixing pipe (3) is connected with a finished product discharging pipe (4).
2. The chemical liquid diversion spiral hedging mixer according to claim 1, wherein: the number of the branch pipes (13) is preferably two; the number of the draft tubes (2) is two.
3. The chemical liquid diversion spiral hedging mixer according to claim 1, wherein: spoilers (11) are arranged in the main pipe (12) of the material shunt pipe (1) in a staggered manner; the top of the material shunt pipe (1) is provided with a material inlet (5).
4. The chemical liquid diversion spiral hedging mixer according to claim 1, wherein: the flow guide pipe (2) is an arc-shaped pipeline.
5. The chemical liquid diversion spiral hedging mixer according to claim 1, wherein: spiral fins (31) are arranged in the spiral opposite-flushing mixing pipe (3).
6. The chemical liquid diversion spiral hedging mixer according to claim 5, wherein: the spiral fins (31) are fixed in the spiral opposite-flushing mixing pipe (3); the helical fin (31) is composed of a central shaft and a fin spirally wound around the central shaft in the axial direction thereof.
7. The chemical liquid diversion spiral hedging mixer according to claim 1, wherein: the middle part of the spiral opposite-flushing mixing pipe (3) is vertically provided with an opening (32); the opening (32) is connected with the finished product discharge pipe (4); and a material opposite-flushing mixing area is arranged right below the opening (32).
8. The chemical liquid diversion spiral hedging mixer according to claim 1, wherein: the finished product discharge pipe (4) is vertically arranged upwards; and the top of the finished product discharge pipe (4) is a finished product outlet (6).
9. The chemical liquid diversion spiral hedging mixer according to claim 1, wherein: the spiral opposite-impact mixing pipe (3) is horizontally arranged.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201911222251.3A CN110756073A (en) | 2019-12-03 | 2019-12-03 | Chemical liquid shunting spiral hedging mixer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201911222251.3A CN110756073A (en) | 2019-12-03 | 2019-12-03 | Chemical liquid shunting spiral hedging mixer |
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CN110756073A true CN110756073A (en) | 2020-02-07 |
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CN201911222251.3A Pending CN110756073A (en) | 2019-12-03 | 2019-12-03 | Chemical liquid shunting spiral hedging mixer |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111393011A (en) * | 2020-04-17 | 2020-07-10 | 徐州创之社通用技术产业研究院有限公司 | Glassware processing and coloring device |
-
2019
- 2019-12-03 CN CN201911222251.3A patent/CN110756073A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111393011A (en) * | 2020-04-17 | 2020-07-10 | 徐州创之社通用技术产业研究院有限公司 | Glassware processing and coloring device |
CN111393011B (en) * | 2020-04-17 | 2023-09-05 | 徐州创之社通用技术产业研究院有限公司 | Glassware processing coloring device |
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