CN210448135U - Internal condensing system of molecular distillation equipment - Google Patents
Internal condensing system of molecular distillation equipment Download PDFInfo
- Publication number
- CN210448135U CN210448135U CN201921163429.7U CN201921163429U CN210448135U CN 210448135 U CN210448135 U CN 210448135U CN 201921163429 U CN201921163429 U CN 201921163429U CN 210448135 U CN210448135 U CN 210448135U
- Authority
- CN
- China
- Prior art keywords
- shunt tubes
- pipe
- feed liquor
- liquor pipe
- shunt
- 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.)
- Active
Links
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides a molecular distillation equipment's inside condensing system, includes feed liquor pipe, a plurality of shunt tubes and solid fixed ring, the shunt tubes sets up in the below of feed liquor pipe and sets up perpendicularly with the feed liquor pipe, the feed liquor pipe is the annular pipe and fixes on molecular distillation equipment's shells inner wall, gu fixed ring sets up in the bottom of a plurality of shunt tubes and fixes a plurality of shunt tubes on the inner wall of casing, wherein be provided with the first throttle of positive V type, the second throttle of the type of falling V respectively on every two adjacent shunt tubes, be provided with the shunt tubes of first throttle pass through the connecting pipe with be provided with the shunt tubes intercommunication of second throttle. The utility model discloses a mode that positive V type and the type of falling V flow controller combined together in a plurality of shunt tubes series connection and the shunt tubes promotes its outflow pressure, makes things convenient for the interior condensation medium that remains of later stage clearance shunt tube simultaneously.
Description
Technical Field
The utility model belongs to distillation mechanical equipment field, concretely relates to molecular distillation equipment's inside condensing system.
Background
Molecular distillation is a special liquid-liquid split technology, which is different from traditional distillation and relies on the principle of boiling point difference separation, but relies on the difference of different substance molecular motion mean free path to realize separation. When the liquid mixture flows along the heating plate and is heated, light and heavy molecules can escape from the liquid surface and enter the gas phase, because of different free paths of the light and heavy molecules, the molecules of different substances move for different distances after escaping from the liquid surface, if a condensing plate can be properly arranged, the light molecules reach the condensing plate and are condensed and discharged, and the heavy molecules cannot reach the condensing plate and are discharged along the mixed liquid, so that the aim of separating the substances is fulfilled. The advantages of molecular distillation are: the distillation temperature is low, the molecular distillation is operated at a temperature far lower than the boiling point, and the separation can be achieved as long as the temperature difference exists, which is the essential difference between the molecular distillation and the conventional distillation; the distillation vacuum degree is high, the molecular distillation device can obtain high vacuum degree in the molecular distillation device, and the molecular distillation is usually operated under low pressure, so that materials are not easy to oxidize and damage; the distilled liquid film is thin, and the heat transfer efficiency is high; the heating time of the material is short, the distance between the heated liquid surface and the condensing surface is less than the mean free path of the light molecules, so the light molecules escaping from the liquid surface almost reach the condensing surface without collision, therefore, the heating time of the distillation material is short, the retention time at the distillation temperature is generally between several seconds and dozens of seconds, and the chance of material decomposition is reduced; the separation degree is higher, and the molecular distillation can separate substances which are not easy to separate conventionally.
Among the prior art, condensing equipment generally adopts is whole liquid chamber, can store a large amount of condensing medium, has nevertheless also caused the waste simultaneously, and some condensing medium prices are more expensive, and a large amount of uses can increase the cost, and the use of another kind of condensing medium can be influenced in the remaining of another kind of condensing medium, the effect of condensing promptly, therefore the clearance of later stage condenser pipe also is a problem that needs to solve.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving the problem and providing an internal condensing system of molecular distillation equipment.
The technical scheme of the utility model is that: the utility model provides a molecular distillation equipment's inside condensing system, includes feed liquor pipe, a plurality of shunt tubes and solid fixed ring, the shunt tubes sets up in the below of feed liquor pipe and sets up perpendicularly with the feed liquor pipe, the feed liquor pipe is the annular pipe and fixes on molecular distillation equipment's shells inner wall, gu fixed ring sets up in the bottom of a plurality of shunt tubes and fixes a plurality of shunt tubes on the inner wall of casing, wherein be provided with the first throttle of positive V type, the second throttle of the type of falling V respectively on every two adjacent shunt tubes, be provided with the shunt tubes of first throttle pass through the connecting pipe with be provided with the shunt tubes intercommunication of second throttle.
Further optimize, feed liquor pipe and solid fixed ring are two rings shape that the diameter is the same, and feed liquor pipe and solid fixed ring are partial upper and lower in shells inner wall.
Further optimize, the upper and lower part of every shunt tubes all is provided with the connecting pipe, and this connecting pipe all is used for communicateing adjacent shunt tubes.
Further optimize, the feed liquor pipe is gone up and is begun to have the inlet, the inlet is embedded to have the pipeline, and this pipeline gos deep into in one of them shunt tubes to realize coolant's the letting in through the pipeline, be provided with the through-hole with another shunt tubes upper end that above-mentioned shunt tubes are adjacent, through this through-hole condensate medium flow to in the feed liquor pipe, and flow out through the egress opening of feed liquor pipe.
The utility model has the advantages that:
the condensing device is arranged on the inner wall of a distiller shell through a fixing ring in a mode of serially connecting a plurality of liquid inlet pipes, a positive V-shaped first throttleer and an inverted V-shaped second throttleer are respectively arranged in two adjacent liquid inlet pipes, condensing media enter a shunt pipe from the liquid inlet pipe above the shunt pipe, enter a small flow and are discharged, so that the outflow pressure of the condensing media is increased, the temperature difference in the shell is ensured, the separation effect is improved, and meanwhile, the residual condensing media in the shunt pipe at the later stage are convenient to wash;
secondly, a pipeline is arranged in a liquid inlet of the liquid inlet pipe, the condensing medium is directly conveyed into one of the shunt pipes through the pipeline, the shunt pipe transmits the condensing medium into the adjacent shunt pipe through a connecting pipe until the condensing medium is transmitted into the last shunt pipe, meanwhile, the gas in the pipe is pushed by the condensing medium until the gas in the last shunt pipe is discharged through a vent hole, and the vent hole is covered with a non-adhesive waterproof breathable film, so that the phenomenon that the condensing medium is discharged along with the gas is effectively prevented;
to sum up, the utility model discloses simple, the convenient operation of processing technology adopts the interior positive V type of a plurality of shunt tubes series connection and shunt tubes and the mode that the type of falling V flow controller combined together to promote its outflow pressure, makes things convenient for the interior condensation medium that remains of later stage clearance shunt tubes simultaneously.
Drawings
FIG. 1 is a schematic structural diagram of the present invention
FIG. 2 is a schematic view of the top view structure of the present invention
FIG. 3 is a schematic view of a condensing unit
Reference numerals: 1. feed liquor pipe, 2, shunt tubes, 3, solid fixed ring, 4, casing, 5, first flow controller, 6, second flow controller, 7, connecting pipe, 8, inlet, 9, egress opening, 10, through-hole.
Detailed Description
The technical solutions in the embodiments of the present invention will be eliminated and fully described below with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
An internal condensing system of molecular distillation equipment is provided, which comprises the following specific embodiments: the condensing device comprises a liquid inlet pipe 1, a plurality of shunt pipes 2 and a fixing ring 3, wherein the shunt pipes 2 are arranged below the liquid inlet pipe 1 and are perpendicular to the liquid inlet pipe 1, the liquid inlet pipe 1 is an annular pipe and is fixed on the inner wall of a shell 4, the fixing ring 3 is arranged at the bottoms of the shunt pipes 2 and fixes the shunt pipes 2 on the inner wall of the shell 4, wherein a positive V-shaped first throttle 5 and an inverted V-shaped second throttle 6 are respectively arranged on every two adjacent shunt pipes 2, the shunt pipe 2 provided with the positive V-shaped first throttle 5 is communicated with the shunt pipe 2 provided with the second throttle 6 through a connecting pipe 7, condensing media enter the shunt pipe 2 from the liquid inlet pipe 1 above the shunt pipe, enter into a small flow and are discharged, so that the outflow pressure of the condensing media is increased, the temperature difference in the shell 4 is ensured, and the separation effect is improved, meanwhile, the residual condensing medium in the later-stage flow dividing pipe 2 is convenient to flush; feed liquor pipe 1 and solid fixed ring 3 are two rings shape that the diameter is the same, and feed liquor pipe 1 and solid fixed ring 3 divide and lie in two upper and lower parts of 4 inner walls of casing, feed liquor pipe 1 and solid fixed ring 3.
The feed liquor pipe 1 is gone up and is begun to have the inlet 8, 8 embedded pipelines that have of inlet, this pipeline is deepened in one of them shunt tubes 2, every shunt tubes 2 upper and lower two parts all are provided with connecting pipe 7, this connecting pipe 7 all is used for communicateing adjacent shunt tubes 2, condensing medium passes through the interior pipeline of inlet 8 and directly gets into shunt tubes 2, in the high-speed transmission of the first flow controller 5 that contains positive V type arrives adjacent second flow controller 6 of falling V type, at last with gas along with condensing medium through-hole 10 flow to feed liquor pipe 1 in, discharge by egress opening 9 at last.
The essential features, method of use, working process, basic principles and advantages of the invention have been shown and described above. It should be understood by those skilled in the art that the present invention is not limited to the above embodiments, and the above embodiments and descriptions are only illustrative of the principles of the present invention, and that the present invention can be modified in various ways according to the actual situation without departing from the spirit and scope of the present invention, and these modifications and improvements are all within the scope of the present invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (4)
1. An internal condensing system of molecular distillation equipment, characterized in that: including feed liquor pipe (1), a plurality of shunt tubes (2) and solid fixed ring (3), shunt tubes (2) set up in the below of feed liquor pipe (1) and set up perpendicularly with feed liquor pipe (1), feed liquor pipe (1) is the annular pipe and fixes on the casing (4) inner wall of molecular distillation equipment, gu fixed ring (3) set up in the bottom of a plurality of shunt tubes (2) and fix a plurality of shunt tubes (2) on the inner wall of casing (4), wherein be provided with first throttle (5) of positive V type, the second throttle (6) of the type of falling V on every two adjacent shunt tubes (2) respectively, be provided with shunt tubes (2) of first throttle (5) through connecting pipe (7) with be provided with shunt tubes (2) intercommunication of second throttle (6).
2. An internal condensation system for a molecular distillation apparatus according to claim 1, wherein: feed liquor pipe (1) and solid fixed ring (3) are two rings shape that the diameter is the same, and feed liquor pipe (1) and solid fixed ring (3) are separated in the upper and lower part of casing (4) inner wall.
3. An internal condensation system for a molecular distillation apparatus according to claim 1, wherein: the upper part and the lower part of each shunt pipe (2) are respectively provided with a connecting pipe (7), and the connecting pipes (7) are used for communicating the adjacent shunt pipes (2).
4. An internal condensation system for a molecular distillation apparatus according to claim 1, wherein: the utility model discloses a cooling medium's structure, including feed liquor pipe (1), inlet (8) are gone up and are begun to have inlet (8), inlet (8) are embedded to have the pipeline, and this pipeline is gone deep into in one of them shunt tubes (2) to realize coolant's letting in through the pipeline, another shunt tubes (2) upper end adjacent with above-mentioned shunt tubes (2) is provided with through-hole (10), and in through this through-hole (10) condensate medium flows to the inlet pipe, and flow outlet (9) through feed liquor pipe (1) are flowed out.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921163429.7U CN210448135U (en) | 2019-07-23 | 2019-07-23 | Internal condensing system of molecular distillation equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921163429.7U CN210448135U (en) | 2019-07-23 | 2019-07-23 | Internal condensing system of molecular distillation equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN210448135U true CN210448135U (en) | 2020-05-05 |
Family
ID=70447041
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201921163429.7U Active CN210448135U (en) | 2019-07-23 | 2019-07-23 | Internal condensing system of molecular distillation equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN210448135U (en) |
-
2019
- 2019-07-23 CN CN201921163429.7U patent/CN210448135U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104759108A (en) | Three-stage continuous falling-film circulating evaporation concentration system with machinery vapor recompression | |
CN204522328U (en) | Three grades with function of mechanical steam recompression continuous falling liquid film circulating and evaporating concentration systems | |
CN105107225A (en) | Multifunctional extraction tank | |
CN210448135U (en) | Internal condensing system of molecular distillation equipment | |
CN102266677B (en) | High vacuum distillation purification device | |
US20230311024A1 (en) | Cooling device and cooling method for maltol sublimation section | |
CN109708495A (en) | Hot waste water waste-heat recovery device during textile dyeing final finishing | |
CN205391788U (en) | Waste gas recovery heat transfer system | |
CN203862234U (en) | Multifunctional reaction system | |
CN210434013U (en) | A molecular distillation equipment for rosemary hydrolat draws | |
CN105617707A (en) | Exhaust gas recycling and heat exchange system | |
CN204944228U (en) | A kind of condenser avoiding fixed gas to gather | |
CN209809546U (en) | Split type end effect evaporator with water cooling function | |
CN111375220B (en) | Gas-liquid separation and recovery device | |
CN102221191A (en) | Secondary steam generator | |
CN205164164U (en) | Tape unit tool vapor recompression's tertiary concentrated system of falling liquid film circulation evaporating in succession | |
CN210097680U (en) | Reation kettle vapor recovery system | |
CN104826348A (en) | Extraction mixed liquor treatment method by recycling steam condensate waste heat | |
CN203710719U (en) | Cyclization reaction dehydrating device | |
CN203002009U (en) | Heat-exchange gas-liquid separator | |
CN211411021U (en) | Material evaporator with liquid level balancing function | |
CN219615204U (en) | Condensing reflux device | |
RU96641U1 (en) | DEVICE FOR HEAT EXCHANGE PROCESSES | |
CN212687608U (en) | Vacuum treatment system and sewage treatment system | |
CN218376884U (en) | Vacuum pump evacuation steam recovery unit |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |