CN201632260U - Evaporation mixer - Google Patents
Evaporation mixer Download PDFInfo
- Publication number
- CN201632260U CN201632260U CN2010201341496U CN201020134149U CN201632260U CN 201632260 U CN201632260 U CN 201632260U CN 2010201341496 U CN2010201341496 U CN 2010201341496U CN 201020134149 U CN201020134149 U CN 201020134149U CN 201632260 U CN201632260 U CN 201632260U
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- CN
- China
- Prior art keywords
- evaporation
- piece
- sleeve pipe
- pipe
- part block
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Abstract
The utility model provides an evaporation mixer, which is characterized by comprising an evaporation mixing part block, wherein the periphery of the evaporation mixing part block is wrapped with a heating part block, the inside of the evaporation mixing part block is filled with packing, and the middle part in the evaporation mixing part block is provided with a sleeve pipe; the top of the inner pipe of the sleeve pipe is blocked, the side wall of the upper part of the sleeve pipe is provided with a groove or a hole, and the bottom of the sleeve pipe is connected with a three-way connector; the side of the three-way connector is connected with a gas-phase material feed pipe; a liquid-phase material feed pipe passes through the three-way connector and then is connected with the inner pipe of the sleeve pipe; the bottom of the evaporation mixing part block is provided with a support part block; and the top of the evaporation mixing part block is connected with a discharge part block. The utility model has the advantages of simple structure, high efficiency, small layout space, convenient control, space-and-cost-saving and the like, and has wide application.
Description
Technical field
The utility model relates to a kind of evaporation mixing apparatus.
Background technology
Usually need in the chemical engineering experiment device liquid is evaporated to gas and is mixed into reactor reaction with unclassified stores.Current technology is to use for reference industrial practice, by a heat exchanger liquid is evaporated, and mixes with gaseous phase materials then.This mode mainly contains 4 deficiencies: 1, because heat exchanger mostly is tubulation or single pipe heat exchanger, and the time of staying is short therein, heat transfer area is limited for liquid phase material, in order to reach the purpose that is gasified totally, heat exchanger is usually done very greatly.2, the liquid-phase vaporization product mixes with cold gaseous phase materials and easily causes the vaporizer condensation, and mixed temperature of charge should not be controlled, thereby gaseous phase materials need add preheater in addition before mixing.3, in order to reach the uniform purpose of mixing of materials, need establish blender in addition.4, evaporation hybrid system module is disperseed, and has not only increased equipment investment, and needs more arrangement space.Above deficiency greatly reduces the efficient and the practicality of evaporation mixer.
Summary of the invention
The purpose of this utility model provides a kind of raising the efficiency and the evaporation mixing apparatus of practicality.
In order to achieve the above object, the technical solution of the utility model has provided a kind of evaporation mixer, it is characterized in that, comprise evaporation mixing portion piece, around evaporation mixing portion piece, be enclosed with the heating part piece, in evaporation mixing portion piece, be filled with filler, the middle part is provided with sleeve pipe in evaporation mixing portion piece, the top of pipe is stopped up in the sleeve pipe, has groove or hole on the sidewall at an upper portion thereof, and the bottom of sleeve pipe is connected with three-way connection, the three-way connection side is connected with the gaseous phase materials feed pipe, the liquid phase material feed pipe passes to manage in three-way connection and the sleeve pipe and links to each other, and is provided with the seat part piece in the bottom of evaporation mixing portion piece, and the top of evaporation mixing portion piece links to each other with the discharging portion piece.
Further, on described discharging portion piece, be provided with the tracing thermal-insulating device.
Be connected with cutting ferrule, screw thread or bump joint on the top of described discharging portion piece.
The utility model has solved in the experimental provision big flow liquid phase rapid evaporation mixed problem, compared with prior art, has simple structure, efficient height, arrangement space is little, control is convenient, advantages such as saving space and cost.When gas-liquid two-phase feeding, can use as evaporation mixer; When having only gas-phase feed, can use as preheater; When having only liquid phase feeding, can use as evaporation/preheater, as steam generator.Thereby the utility model is widely used.
Description of drawings
The structural representation of a kind of evaporation mixer that Fig. 1 provides for the utility model;
Fig. 2 is sleeve pipe sidewall fluting schematic diagram;
Fig. 3 is a sleeve pipe side-wall hole schematic diagram.
The specific embodiment
Specify the utility model below in conjunction with embodiment.
As shown in Figure 1, a kind of evaporation mixer that provides for this utility model, comprise evaporation mixing portion piece 1, around evaporation mixing portion piece 1, be enclosed with heating part piece 2, in evaporation mixing portion piece 1, be filled with filler, the middle part is provided with sleeve pipe 3 in evaporation mixing portion piece 1, the top of pipe is stopped up in the sleeve pipe 3, have groove 5 or hole 6 on the sidewall at an upper portion thereof, the bottom of sleeve pipe 3 is connected with three-way connection 7, and three-way connection 7 sides are connected with gaseous phase materials feed pipe 8, and liquid phase material feed pipe 9 passes three-way connection 7 and links to each other with pipe in the sleeve pipe 3, bottom at evaporation mixing portion piece 1 is provided with seat part piece 10, and the top of evaporation mixing portion piece 1 links to each other with discharging portion piece 11.
Gas enters evaporation mixing portion piece 1 bottom by the shell clearance of sleeve pipe 3; Liquid phase material feed pipe 9 is the interior pipe of sleeve pipe 3, directly passes three-way connection 7, enters the top of evaporation mixing portion piece 1, thereby realizes that gas-liquid two-phase separates charging.The top of pipe is stopped up in the sleeve pipe 3, as shown in Figure 2, on its sidewall, slot 5, the width of groove 5 is less than the diameter of filler in the evaporation mixing portion piece 1, the gross area of groove is not less than the circulation area of pipe in the sleeve pipe 3, and the position of groove is heated to the required heat exchange area decision of drop temperature by liquid phase material from its saturation temperature.
Evaporation mixing portion piece 1 is a container of filling filler, and for the heat of external heat portion piece 2 can in time pass to the center fast, the internal diameter of container is unsuitable excessive.The liquid material that enters from top, under the effect of gravity, by the distribution of filler, the limit disperses toward the current downflow limit, and carburation by evaporation simultaneously is heated.The limit of up flowing, the gaseous phase materials limit that enters from the bottom is heated intensification, and mixes the mobile distribution effect of liquid in filler that also strengthened of gaseous phase materials with product after the liquid phase vaporization.Thereby filler is the important component part of evaporation mixing portion piece 1, has not only increased heat transfer area, and has played the liquid distribution effect, has also increased the less turbulence of mixing of materials.Filler has good thermal conductivity and corrosion resistance, by charging aperture or discharging opening loading and unloading.
Discharging portion piece 11 is a pipeline, is furnished with cutting ferrule, screw thread or bump joint, and convenience is connected with rear module.In order to eliminate the heat loss of mixed material in pipeline is carried after the vaporization, discharge pipe needs pipeline heat insulation/companion heat, so tracing thermal-insulating device 12 is set.
Heating part piece 2 is for providing the parts of thermal source to evaporation mixer, form can be electric furnace, heating jacket, heating tape etc.Heating part piece 2 is installed on the device frame by the side journal stirrup.
As shown in Figure 3, the difference of present embodiment and embodiment 1 is, perforate 6 on the sidewall of sleeve pipe 3, the diameter in hole 6 is less than the diameter of filler in the evaporation mixing portion piece 1, the gross area in hole is not less than the circulation area of pipe in the sleeve pipe 3, and the position in hole is heated to the required heat exchange area decision of drop temperature by liquid phase material from its saturation temperature.Other structures and working method are identical with embodiment 1.
Claims (3)
1. evaporation mixer, it is characterized in that, comprise evaporation mixing portion's piece (1), be enclosed with heating part piece (2) all around at evaporation mixing portion's piece (1), in evaporation mixing portion's piece (1), be filled with filler, the middle part is provided with sleeve pipe (3) in evaporation mixing portion's piece (1), the top of the interior pipe of sleeve pipe (3) is stopped up, have groove (5) or hole (6) on the sidewall at an upper portion thereof, the bottom of sleeve pipe (3) is connected with three-way connection (7), three-way connection (7) side is connected with gaseous phase materials feed pipe (8), liquid phase material feed pipe (9) passes three-way connection (7) and links to each other with pipe in the sleeve pipe (3), bottom at evaporation mixing portion's piece (1) is provided with seat part piece (10), and the top of evaporation mixing portion's piece (1) links to each other with discharging portion piece (11).
2. a kind of evaporation mixer as claimed in claim 1 is characterized in that, is provided with tracing thermal-insulating device (12) on described discharging portion piece (11).
3. a kind of evaporation mixer as claimed in claim 1 is characterized in that, is connected with cutting ferrule, screw thread or bump joint on the top of described discharging portion piece (11).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010201341496U CN201632260U (en) | 2010-02-25 | 2010-02-25 | Evaporation mixer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010201341496U CN201632260U (en) | 2010-02-25 | 2010-02-25 | Evaporation mixer |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201632260U true CN201632260U (en) | 2010-11-17 |
Family
ID=43076732
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010201341496U Expired - Lifetime CN201632260U (en) | 2010-02-25 | 2010-02-25 | Evaporation mixer |
Country Status (1)
Country | Link |
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CN (1) | CN201632260U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101733062B (en) * | 2010-02-25 | 2012-01-18 | 迈瑞尔实验设备(上海)有限公司 | Evaporation mixer |
-
2010
- 2010-02-25 CN CN2010201341496U patent/CN201632260U/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101733062B (en) * | 2010-02-25 | 2012-01-18 | 迈瑞尔实验设备(上海)有限公司 | Evaporation mixer |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20101117 Effective date of abandoning: 20120118 |