CN206198728U - A kind of spiral distillation cascade - Google Patents
A kind of spiral distillation cascade Download PDFInfo
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- CN206198728U CN206198728U CN201621217083.0U CN201621217083U CN206198728U CN 206198728 U CN206198728 U CN 206198728U CN 201621217083 U CN201621217083 U CN 201621217083U CN 206198728 U CN206198728 U CN 206198728U
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- main pipe
- tube
- spiral
- distillation cascade
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Abstract
The utility model provides a kind of spiral distillation cascade, including main pipe, helix tube；It is hollow tube in described main pipe, described main pipe one end is provided with into the mouth of pipe；Described helix tube includes outer spiral tube；Described outer spiral tube is wound in main pipe outside；Described main pipe is provided with connector；Described outer spiral tube is connected with described main pipe by described connector；Described outer spiral tube one end is connected with outlet spout.The coolant that the utility model meets rapid large-area distillation is collected, while the design of pressure-reducing valve reduces overpressure, container ruptures caused by preventing overpressure too high.The utility model design is ingenious, practical, is easy to promote.
Description
Technical field
The utility model is related to evaporation equipment field, and in particular to a kind of spiral distillation cascade.
Background technology
Distillation is a kind of thermodynamic (al) separating technology, and it is different using each component boiling point in mixing liquid or liquid-solid system,
Low boiling component is evaporated, then condenses to separate the unit process of whole component, be to evaporate and condense two kinds of unit operations
Joint.With other separation means, such as extraction, filtering for crystallizing compare, its advantage be without the use of system components with
Other outer solvents, so as to ensure that new impurity will not be introduced.Distillation cascade is the conventional vessel of solution distillation, common distillation cascade
Structure is single, it is impossible to which the coolant for meeting rapid large-area distillation is collected.
Utility model content
The purpose of this utility model is the problem above for overcoming prior art to exist, there is provided a kind of spiral distillation cascade.
To realize above-mentioned technical purpose, above-mentioned technique effect is reached, the utility model is achieved through the following technical solutions：
A kind of spiral distillation cascade, including distillation cascade, described distillation cascade include main pipe, helix tube；Described main pipe
Interior is hollow tube, and described main pipe one end is provided with into the mouth of pipe；Described helix tube includes outer spiral tube；Described outer spiral tube
It is wound in main pipe outside；Described main pipe is provided with connector；Described outer spiral tube passes through institute with described main pipe
The connector connection stated；Described outer spiral tube one end is connected with outlet spout.
Further, it is provided with pressure-reducing valve at described outlet spout.
Further, described main pipe is additionally provided with a connecting hole, and described main pipe connects through institute with distillation equipment
The connecting hole stated coordinates with connecting pole.
Further, described main pipe is additionally provided with an at least fixing hole, and described main pipe is by described fixing hole
It is fixedly connected with distillation equipment.
Further, described main pipe is additionally provided with a spacing hole, and described spacing hole coordinates limitation described with spacer pin
Outer spiral tube position.
Further, it is provided with a cut-off inside described main pipe；Main pipe is separated into two independences by described cut-off
Space；Described the enter mouth of pipe, outlet spout, connector is located at described cut-off homonymy.
Further, riffled tube, inlet connecting branch are provided with inside described main pipe；Described riffled tube spiral cloth
It is placed in inside main pipe；Described riffled tube one end is connected by inlet connecting branch with the mouth of pipe is entered, and the other end passes through connector
It is connected with outer spiral tube.
Further, the material of described outer spiral tube is glass or resin；The material of described riffled tube is glass
Or resin.
The beneficial effects of the utility model are:The utility model provides a kind of spiral distillation cascade, including main pipe, spiral
Pipe；It is hollow tube in described main pipe, described main pipe one end is provided with into the mouth of pipe；Described helix tube includes external spiral
Pipe；Described outer spiral tube is wound in main pipe outside；Described main pipe is provided with connector；Described outer spiral tube and institute
The main pipe for stating is connected by described connector；Described outer spiral tube one end is connected with outlet spout.The utility model meets
The coolant of rapid large-area distillation is collected, while the design of pressure-reducing valve reduces overpressure, prevents that overpressure is too high to be caused
Container ruptures.The utility model design is ingenious, practical, is easy to promote.
Described above is only the general introduction of technical solutions of the utility model, in order to better understand skill of the present utility model
Art means, and being practiced according to the content of specification, with preferred embodiment of the present utility model and coordinate accompanying drawing detailed below
Describe in detail bright as after.Specific embodiment of the present utility model is shown in detail by following examples and its accompanying drawing.
Brief description of the drawings
Accompanying drawing described herein is used for providing being further understood to of the present utility model, constitutes the part of the application,
Schematic description and description of the present utility model is used to explain the utility model, does not constitute to of the present utility model improper
Limit.In the accompanying drawings：
Fig. 1 is a kind of spiral distillation cascade schematic diagram of the present utility model；
Fig. 2 is a kind of distilling apparatus overall schematic；
Fig. 3 is a kind of spiral distillation cascade internal view of the present utility model；
Fig. 4 is another spiral distillation cascade internal view of the present utility model；
Fig. 5 is to use a kind of distilling apparatus structural representation Fig. 1 of the present utility model；
Fig. 6 is to use a kind of distilling apparatus structural representation Fig. 2 of the present utility model；
Fig. 7 is to use a kind of distilling apparatus structural representation Fig. 3 of the present utility model；
Fig. 8 is that the utility model is connected top schematic diagram with a kind of distilling apparatus；
Fig. 9 is that the utility model is connected bottom schematic diagram with a kind of distilling apparatus；
Label declaration in figure：Base 1, foot pad 11, hollow-out parts 12, master control post 2, control panel 21, heater 3, intensification bottle 4,
First body 41, the second body 42, fixed column 51, whirligig 52, connecting pole 53, toroidal frame 54, spacer pin 55, linking arm
57th, distillation cascade 6, enter the mouth of pipe 61, outer spiral tube 62, outlet spout 63, fixing hole 64, connector 65, cut-off 66, riffled tube 67,
Inlet connecting branch 68, connecting hole 69, spacing hole 691, liquid-collecting bottle 7, liquid collection opening 71, exhaust outlet 72.
Specific embodiment
Describe the utility model in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
Shown in reference picture 1-9, a kind of spiral distillation cascade, including distillation cascade 6, described distillation cascade 6 includes main pipe, spiral
Pipe；It is hollow tube in described main pipe, described main pipe one end is provided with into the mouth of pipe 61；Described helix tube includes external spiral
Pipe 62；Described outer spiral tube 62 is wound in main pipe outside；Described main pipe is provided with connector 65；Described external spiral
Pipe 62 is connected with described main pipe by described connector 65；Described one end of outer spiral tube 62 is connected with outlet spout 63.
Preferably, as shown in figure 1, being provided with pressure-reducing valve at described outlet spout 63.Preferably, described main pipe is additionally provided with
One connecting hole 69, described main pipe connects through described connecting hole 69 and coordinates with connecting pole 53 with distillation equipment.Preferably,
As shown in figure 8, described main pipe is additionally provided with an at least fixing hole 64, described main pipe is by described fixing hole 64 and steaming
The equipment of evaporating is fixedly connected.
Preferably, as shown in figure 9, described main pipe is additionally provided with a spacing hole 691, described spacing hole 691 with it is spacing
Pin 55 coordinates the position of outer spiral tube 62 described in limitation.
Preferably, as shown in figure 3, being provided with a cut-off 66 inside described main pipe；Described cut-off 66 divides main pipe
It is divided into two separate spaces；Described the enter mouth of pipe 61, outlet spout 63, connector 65 is located at the described homonymy of cut-off 66.
Preferably, as shown in figure 4, being provided with riffled tube 67, inlet connecting branch 68 inside described main pipe；Described is interior
The screw arrangement of screwed pipe 67 is inside main pipe；Described one end of riffled tube 67 is connected by inlet connecting branch 68 with the mouth of pipe 61 is entered
Connect, the other end is connected by connector 65 with outer spiral tube 62.
Preferably, the material of described outer spiral tube 62 is glass or resin；The material of described riffled tube 67 is glass
Glass or resin.
A kind of distilling apparatus, as shown in Fig. 2 including base 1, master control post 2, heater 3, intensification bottle 4, pillar 5, distillation cascade
6th, liquid-collecting bottle 7；Described master control post 2, pillar 5 are individually fixed on described base 1；Control is provided with described master control post 2
Device；Described heater 3 is connected with described master control post 2, and described distillation cascade 6 is fixed on described pillar 5；Described liter
Warm bottle 4 is positioned over the described top of heater 3；Described intensification bottle 4 is connected with described distillation cascade 6；Described distillation cascade 6 with
Described liquid-collecting bottle 7 is connected；Described controller control heater 3 heats described intensification bottle 4, is mixed in described intensification bottle 4
Solution is closed to be collected in liquid-collecting bottle 7 through the distillation cascade 6.As shown in fig. 6, the upper end of master control post 2 is provided with control panel 21, control panel 21
It is connected with controller, the heat temperature raising of 21 heater of operation control panel 3 bottle 4.
Preferably, described pillar 5 is provided with fixed column 51；Whirligig 52 is provided with described fixed column 51；Described
Whirligig 52 is by controller control；Described intensification bottle 4 is inclined；As shown in fig. 7, described intensification bottle 4 includes the first body
41st, the second body 42；Whirligig 52 of described the first body 41, the second body 42 described in is tightly connected；Described
Whirligig 52 drives the second described body 42 to rotate.The first described body 41 is provided with gas outlet, gas outlet and inlet pipe
Mouth 61 is connected.
Preferably, as shown in figure 5, described liquid-collecting bottle 7 is positioned on toroidal frame 54；Described toroidal frame 54 is by described
Connecting pole 53 be connected with master control post 2.As shown in fig. 7, described heater 3 is connected with master control post 2 by linking arm 57.
Preferably, as described in Figure 5, the described bottom of base 1 is provided with foot pad 11, hollow-out parts 12, and foot pad 11 prevents base from grinding
Damage, it is preferable that base 1 is made up of casting, and hollow-out parts 12 can mitigate constant weight, while the weight of base 1 can also fill distillation
The center of gravity reduction put.
Preferably, as described in Figure 6, liquid-collecting bottle 7 is provided with liquid collection opening 71, exhaust outlet 72；After being condensed through described distillation cascade 6,
The liquid of distillation flows out to liquid collection opening 71 from outlet spout 63, is collected in liquid-collecting bottle 7, and the design of exhaust outlet 72 prevents liquid-collecting bottle 7
Interior air pressure increases always.
The utility model provides a kind of spiral distillation cascade, including main pipe, helix tube；It is hollow in described main pipe
Pipe, described main pipe one end is provided with into the mouth of pipe；Described helix tube includes outer spiral tube；Described outer spiral tube is wound in master
Body outside；Described main pipe is provided with connector；Described outer spiral tube is with described main pipe by described connection
Mouth connection；Described outer spiral tube one end is connected with outlet spout.The coolant that the utility model meets rapid large-area distillation is received
Collection, while the design of pressure-reducing valve reduces overpressure, container ruptures caused by preventing overpressure too high.The utility model is designed
It is ingenious, it is practical, it is easy to promote.
The above, preferred embodiment only of the present utility model not makees any formal to the utility model
Limitation；The those of ordinary skill of all industry can shown in by specification accompanying drawing and the above and swimmingly implement this practicality
It is new；But, all those skilled in the art are not being departed from the range of technical solutions of the utility model, are taken off more than
The technology contents for showing and the equivalent variations of a little variation, modification and evolution made, are Equivalent embodiments of the present utility model；
Meanwhile, the change of all any equivalent variations made to above example according to substantial technological of the present utility model, modify and drill
Become etc., still fall within the protection domain of the technical solution of the utility model.
Claims (8)
1. a kind of spiral distillation cascade, including distillation cascade (6), described distillation cascade (6) includes main pipe, helix tube, and its feature exists
In：It is hollow tube in described main pipe, described main pipe one end is provided with into the mouth of pipe (61)；Described helix tube includes outer spiral shell
Coil (62)；Described outer spiral tube (62) is wound in main pipe outside；Described main pipe is provided with connector (65)；It is described
Outer spiral tube (62) and described main pipe connected by described connector (65)；Described outer spiral tube (62) one end connects
It is connected to outlet spout (63).
2. a kind of spiral distillation cascade according to claim 1, it is characterised in that：Described outlet spout (63) place is provided with decompression
Valve.
3. a kind of spiral distillation cascade according to claim 1, it is characterised in that：Described main pipe is additionally provided with a connecting hole
(69), described main pipe connects through described connecting hole (69) and coordinates with connecting pole (53) with distillation equipment.
4. a kind of spiral distillation cascade according to claim 1, it is characterised in that：Described main pipe is additionally provided with least one and consolidates
Determine hole (64), described main pipe is fixedly connected by described fixing hole (64) with distillation equipment.
5. a kind of spiral distillation cascade according to claim 1, it is characterised in that：Described main pipe is additionally provided with a spacing hole
(691), described spacing hole (691) coordinates outer spiral tube (62) position described in limitation with spacer pin (55).
6. according to a kind of one of them described spiral distillation cascade of claim 1 to 5, it is characterised in that：In described main pipe
Portion is provided with a cut-off (66)；Main pipe is separated into two separate spaces by described cut-off (66)；Described enters the mouth of pipe (61), goes out
The mouth of pipe (63), connector (65) are positioned at described cut-off (66) homonymy.
7. according to a kind of one of them described spiral distillation cascade of claim 1 to 5, it is characterised in that：In described main pipe
Portion is provided with riffled tube (67), inlet connecting branch (68)；Described riffled tube (67) screw arrangement is inside main pipe；It is described
Riffled tube (67) one end be connected with the mouth of pipe (61) is entered by inlet connecting branch (68), the other end by connector (65) with it is outer
Helix tube (62) is connected.
8. a kind of spiral distillation cascade according to claim 7, it is characterised in that：The material of described outer spiral tube (62) is
Glass or resin；The material of described riffled tube (67) is glass or resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621217083.0U CN206198728U (en) | 2016-11-11 | 2016-11-11 | A kind of spiral distillation cascade |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621217083.0U CN206198728U (en) | 2016-11-11 | 2016-11-11 | A kind of spiral distillation cascade |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206198728U true CN206198728U (en) | 2017-05-31 |
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ID=58753072
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621217083.0U Active CN206198728U (en) | 2016-11-11 | 2016-11-11 | A kind of spiral distillation cascade |
Country Status (1)
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|---|---|
| CN (1) | CN206198728U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113499600A (en) * | 2021-07-17 | 2021-10-15 | 海南富山油气化工有限公司 | Intelligent control device used in production process of petroleum mixed xylene |
-
2016
- 2016-11-11 CN CN201621217083.0U patent/CN206198728U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113499600A (en) * | 2021-07-17 | 2021-10-15 | 海南富山油气化工有限公司 | Intelligent control device used in production process of petroleum mixed xylene |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder |
Address after: 215000 No. 388 Shui Shui Road, Suzhou Industrial Park, Jiangsu Patentee after: SUZHOU YACOO SCIENCE Co.,Ltd. Address before: 215000 Changyang street, Suzhou Industrial Park, Jiangsu, China, No. 415, No. Patentee before: SUZHOU YACOO SCIENCE Co.,Ltd. |
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| CP02 | Change in the address of a patent holder |