CN206543419U - A kind of distiller condenser of sub-sectional cooling - Google Patents
A kind of distiller condenser of sub-sectional cooling Download PDFInfo
- Publication number
- CN206543419U CN206543419U CN201720256117.5U CN201720256117U CN206543419U CN 206543419 U CN206543419 U CN 206543419U CN 201720256117 U CN201720256117 U CN 201720256117U CN 206543419 U CN206543419 U CN 206543419U
- Authority
- CN
- China
- Prior art keywords
- tank body
- condensation tank
- condensation
- cooling
- cooling coil
- 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.)
- Expired - Fee Related
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of distiller condenser of sub-sectional cooling, belong to condenser field.It includes condensation tank body, the first cooling coil, the second cooling coil, air chamber, aspiration pump, the condensation tank body is closed tank, air inlet is provided with the top of condensation tank body, first cooling coil is coiled in the top of condensation tank wall, second cooling coil is coiled in the bottom of condensation tank wall, the plenum roof is connected with condensing the bottom of tank body, and described aspiration pump one end is connected by pipeline with plenum roof, and the other end is connected by pipeline with the air inlet on condensation tank body.Coiled respectively using coil pipe in condensation tank body top and the bottom, maintain condensation tank body top and the bottom mutually synthermal, conducted heat in gas condensation process uniform, heat transfer efficiency is high, improves condensation efficiency；Uncooled gas, which is entered, in condensation tank body is evacuated to air inlet by aspiration pump in air chamber and continues to condense, it is to avoid gas loss, improves product yield.
Description
Technical field
The utility model is related to a kind of distiller condenser of sub-sectional cooling, belongs to condenser field.
Background technology
In chemical field, many chemical raw materials or medicine etc. need to be purified, and are generally all that liquid charging stock is filled
Enter in reactor, reacted in reactor or be thermally formed gas, it is higher that gas is passed through in condenser formation purity after condensation
Liquid；There is gas flow pipe road inside condenser, during work, during cooling medium enters condenser from condenser bottom, be full of
Condenser is last from top discharge, gas from condenser overhead enter condenser tubes in cooling medium outside pipeline it is cold
Lower condensation is last from bottom outflow；On the one hand due to cooling medium, temperature gradually rises in condenser uphill process, causes
The heat transfer of gas condensation process is uneven, and condensation effect is poor, and another aspect gas condensed liquid is directly discharged from condenser bottom,
The gas of the non-total condensation of a part can also be discharged simultaneously, cause gas loss, product yield is low.
The content of the invention
Technical problem to be solved in the utility model is：A kind of distiller condenser of sub-sectional cooling is provided, it is solved
The problem of current condenser condensation effect is poor, product yield is low.
Technical problem to be solved in the utility model takes following technical scheme to realize：
A kind of distiller condenser of sub-sectional cooling, it includes condensation tank body, in addition to the first cooling coil, the second cooler pan
Pipe, air chamber, aspiration pump, the condensation tank body are to be provided with air inlet, first cooler pan at the top of closed tank, condensation tank body
Pipe dish is wound on the top of condensation tank wall, and second cooling coil is coiled in the bottom of condensation tank wall, the air chamber
Top is connected with condensing the bottom of tank body, and air chamber bottom is provided with liquid outlet, and described aspiration pump one end passes through pipeline and air chamber top
Portion is connected, and the other end is connected by pipeline with the air inlet on condensation tank body.
As preferred embodiment, cooling medium is passed through in first cooling coil, cooling medium is under the first cooling coil
End is passed through, from upper end discharge.
As preferred embodiment, cooling medium is passed through in second cooling coil, cooling medium is under the second cooling coil
End is passed through, from upper end discharge.
The beneficial effects of the utility model are：Tank body upper disc is condensed around the first cooling coil, lower disc is around the second cooling
Coil pipe, makes uniform, the heat transfer efficiency height that conducted heat in gas condensation process, improves condensation effect；The air accumulation that failed to condensation is in gas
Ceiling portion is evacuated to the continuous condensation of condensation tank body relaying by aspiration pump, it is therefore prevented that gas loss, improves product yield.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure：Tank body 1 is condensed, air inlet 11, the first cooling coil 2, the second cooling coil 3, air chamber 4, liquid outlet 41 is taken out
Air pump 5, pipeline 6.
Embodiment
In order to be easy to understand to technological means of the present utility model, creation characteristic, reached purpose and effect, tie below
Conjunction is specifically illustrating, and the utility model is expanded on further.
As shown in figure 1, a kind of distiller condenser of sub-sectional cooling, it includes condensation tank body 1, the first cooling coil 2, second
Cooling coil 3, air chamber 4, aspiration pump 5, the condensation tank body 1 are closed tank, and the top of condensation tank body 1 is provided with air inlet 11,
First cooling coil 2 is coiled in the top of the condensation outer wall of tank body 1, and second cooling coil 3 is coiled in outside condensation tank body 1
The bottom of wall, the top of air chamber 4 is connected with condensing the bottom of tank body 1, and the bottom of air chamber 4 is provided with liquid outlet 41, the pumping
The one end of pump 5 is connected by pipeline 6 with the top of air chamber 4, and the other end is connected by pipeline 6 with the air inlet 11 on condensation tank body 1, the
Cooling medium is passed through in one cooling coil 2, cooling medium is passed through from the lower end of the first cooling coil 2, from upper end discharge, the second cooling
Cooling medium is passed through in coil pipe 3, cooling medium is passed through from the lower end of the second cooling coil 3, from upper end discharge.
Workflow：The lower end from the first cooling coil 2, the second cooling coil 3 is passed through cooling medium, cooling medium respectively
Make to maintain low temperature in condensation tank body 1, gas is entered from the air inlet 11 on condensation tank body 1 and condensed in condensation tank body 1, and gas is cold
The liquid outlet 41 that formation liquid is flowed into air chamber 4 from the bottom of air chamber 4 after solidifying is discharged, a part of uncooled in condensation tank body 1
Gas, which is entered, to be evacuated to air inlet 11 by aspiration pump 5 after air chamber 4 and condenses again.
The utility model is coiled using coil pipe respectively in condensation tank body 1 outer wall top and the bottom, maintains the top and the bottom of condensation tank body 1
Conducted heat mutually synthermal, in gas condensation process uniform, heat transfer efficiency is high, improves condensation efficiency；Condense uncooled in tank body 1
Gas enter and air inlet 11 is evacuated to by aspiration pump 5 in air chamber 4 continues to condense, it is to avoid gas loss, improve product
Yield.
General principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry it should be appreciated that the utility model is not restricted to the described embodiments, do not depart from the utility model spirit and
On the premise of scope, the utility model also has various changes and modifications, and these changes and improvements both fall within the utility model will
In the range of asking protection.Scope is claimed by appended claims and its equivalent thereof in the utility model.
Claims (3)
1. a kind of distiller condenser of sub-sectional cooling, it includes condensation tank body, it is characterised in that：Also include the first cooling coil,
Second cooling coil, air chamber, aspiration pump, the condensation tank body are to be provided with air inlet at the top of closed tank, condensation tank body, described
First cooling coil is coiled in the top of condensation tank wall, and second cooling coil is coiled under condensation tank wall
Portion, the plenum roof is connected with condensing the bottom of tank body, and air chamber bottom is provided with liquid outlet, and described aspiration pump one end passes through pipe
Road is connected with plenum roof, and the other end is connected by pipeline with the air inlet on condensation tank body.
2. a kind of distiller condenser of sub-sectional cooling according to claim 1, it is characterised in that：First cooling coil
In be passed through cooling medium, cooling medium is passed through from the first cooling coil lower end, from upper end discharge.
3. a kind of distiller condenser of sub-sectional cooling according to claim 1, it is characterised in that：Second cooling coil
In be passed through cooling medium, cooling medium is passed through from the second cooling coil lower end, from upper end discharge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720256117.5U CN206543419U (en) | 2017-03-16 | 2017-03-16 | A kind of distiller condenser of sub-sectional cooling |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720256117.5U CN206543419U (en) | 2017-03-16 | 2017-03-16 | A kind of distiller condenser of sub-sectional cooling |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206543419U true CN206543419U (en) | 2017-10-10 |
Family
ID=59996161
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720256117.5U Expired - Fee Related CN206543419U (en) | 2017-03-16 | 2017-03-16 | A kind of distiller condenser of sub-sectional cooling |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206543419U (en) |
-
2017
- 2017-03-16 CN CN201720256117.5U patent/CN206543419U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203687669U (en) | Acid gas condenser | |
| CN207501713U (en) | A kind of jacketed spiral winded type condenser | |
| CN206543419U (en) | A kind of distiller condenser of sub-sectional cooling | |
| CN203123608U (en) | Vertical type three-section condensation cooler | |
| CN201962271U (en) | Water-saving condensing device of wine container | |
| CN208287533U (en) | A kind of p-phenoxyphenol distillation liquor collecting device | |
| CN218794921U (en) | Fatty acid preceding-stage condenser | |
| CN208814988U (en) | A kind of air-cooled water cooling convolution brewing cooler | |
| CN208026115U (en) | A kind of condensing unit that heat exchange efficiency is high | |
| CN110882553A (en) | Low-temperature vacuum evaporator | |
| CN207095343U (en) | A kind of high efficiency heat exchanger | |
| CN214469459U (en) | Condenser | |
| CN205146191U (en) | Alfol salt synthesizer | |
| CN103991874A (en) | Method and system for purifying trichlorosilane from chlorosilane | |
| CN211284260U (en) | Wax catching device | |
| CN209049051U (en) | A kind of reflux condensation mode second level division box | |
| CN209270877U (en) | A kind of recover synthesizing ammonia steam condensate | |
| CN208139870U (en) | A kind of more effect condensers collected for gaseous product liquefaction | |
| CN207324125U (en) | A kind of glacial acetic acid equipment for purifying | |
| CN207024668U (en) | A kind of energy saving device in furfuryl alcohol production | |
| CN209240522U (en) | Efficient inner-cooled vacuum tank and all-steel radial tyre capsule vacuum system | |
| CN105333749B (en) | Efficient cooling system based on auxiliary solar cooling tower | |
| CN206434880U (en) | Falling film evaporator in the two phase countercurrent flow vertical tube of surrounding tangential admission | |
| CN206146256U (en) | Coke oven gas methane gasification cooling device | |
| CN205974333U (en) | Secondary condensation recovery device of production perfume material furanone |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171010 Termination date: 20210316 |