CN209378484U - A kind of rectifying separation packed tower - Google Patents
A kind of rectifying separation packed tower Download PDFInfo
- Publication number
- CN209378484U CN209378484U CN201920028961.1U CN201920028961U CN209378484U CN 209378484 U CN209378484 U CN 209378484U CN 201920028961 U CN201920028961 U CN 201920028961U CN 209378484 U CN209378484 U CN 209378484U
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- China
- Prior art keywords
- copper pipe
- discharge
- tower
- pipeline
- rectifying
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Abstract
The utility model discloses a kind of rectifying to separate packed tower, including tower body, preheater, liquid distribution trough, condenser, heater and the discharge of steam part being fixed inside tower body, heater is connect with discharge of steam part by pipeline, stripping room is provided between discharge of steam part and liquid distribution trough, liquid distribution trough upper surface is to being provided with rectifying room between tower body top, preheater one side upper end is provided with material liquid import, and another side lower end is connect with liquid distribution trough by pipeline；Pass through setting heat dump and copper pipe a, material liquid is preheated using the waste heat that production process generates, accelerate the rate that material liquid is fractionated in tower body, production energy consumption is reduced, by the way that gas vent is arranged at jet thrust lower end surface edge, prevents the fraction of upper end from entering in jet thrust, jet thrust is caused to be blocked, by setting air pressure relief valve and temperature indicator, prevents temperature is excessively high from air pressure being caused to rise, influence the safety of equipment.
Description
Technical field
The utility model belongs to fractionation extractive technique field, and in particular to a kind of rectifying separation packed tower.
Background technique
Rectifying column is a kind of tower vapor-liquid contacting apparatus for carrying out rectifying, has different wave using each component in mixture
Hair degree, i.e. this different property of the vapour pressure of each component at the same temperature, are transferred to the light component in liquid phase in gas phase, and
Heavy constituent in gas phase is transferred in liquid phase, to realize the purpose of separation.
A kind of existing rectifying separates packed tower, when existing to material liquid progress heating extraction, consumes more energy, and
The problem of not also being fully utilized for the heat in the steam of heating extraction, thus it is proposed that a kind of rectifying separates filler
Tower.
Utility model content
The purpose of this utility model is to provide a kind of rectifying to separate packed tower, mentioned above in the background art to solve
A kind of existing rectifying separates packed tower, when existing to material liquid progress heating extraction, consumes more energy, and is used to heat
The problem of heat in the steam of extraction is not also fully utilized.
To achieve the above object, the utility model provides the following technical solutions: a kind of rectifying separation packed tower, including tower
Body, preheater, liquid distribution trough, condenser, heater and the discharge of steam part being fixed inside the tower body, it is described to add
Hot device is connect with the discharge of steam part by pipeline, is provided with stripping between the discharge of steam part and the liquid distribution trough
Room, the liquid distribution trough upper surface are set to rectifying room, preheater one side upper end is provided between the tower body top
It is equipped with material liquid import, another side lower end is connect with the liquid distribution trough by pipeline, and the preheater inner bottom
It is provided with copper pipe b, lateral surface bottom end is provided with water pump, and the one end the copper pipe b is connect with the pump outlet, in the tower body
Side lower end is surrounded with heat dump, and the heat dump is internally provided with copper pipe a, the one end the copper pipe a and the Pump Suction
Mouth of a river connection, the other end are connect with the copper pipe b by pipeline.
Preferably, the discharge of steam part includes the first endless tube and the second endless tube, first endless tube and second ring
Pipe is connected by pipeline, and first endless tube and second endless tube lower end surface are surrounded with multiple equally distributed jets
Head, the jet thrust lower end surface middle part are provided with air inlet supervisor, and lower end surface edge is surrounded with multiple gas vents.
Preferably, the copper pipe a is spiral-shaped structure, and the copper pipe b is " S " type structure.
Preferably, the heat dump lower end is provided with tower bottom cone tank, and tower bottom cone tank bottom end is provided with discharge outlet,
And the heater is connect by pipeline with the discharge outlet air-tightness.
Preferably, preheater upper surface side is provided with air pressure relief valve, and middle part is provided with temperature indicator.
Compared with prior art, the utility model has the beneficial effects that
By setting heat dump and copper pipe a, material liquid is preheated using the waste heat that production process generates, accelerates raw material
The rate that liquid is fractionated in tower body reduces production energy consumption.
By the way that gas vent is arranged at jet thrust lower end surface edge, prevents the fraction of upper end from entering in jet thrust, cause to spray
Gas head is blocked, and by the way that tower bottom cone tank is arranged, convenient for collecting and heating fraction again, passes through setting air pressure relief valve and temperature
Display is spent, prevents temperature is excessively high from air pressure being caused to rise, influences the safety of equipment.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the preheater section view figure structure schematic representation of the utility model；
Fig. 3 is the copper pipe a front view structural representation of the utility model；
Fig. 4 is the vertical view figure structure schematic representation of the utility model；
Fig. 5 is that section view figure structure schematic representation is responsible in the air inlet of the utility model；
Fig. 6 is that the discharge of steam part of the utility model looks up figure structure schematic representation；
In figure: 1, tower body；2, material liquid import；3, preheater；4, water pump；5, tower bottom cone tank；6, heat dump；7, copper pipe
a；8, heater；9, discharge of steam part；10, stripping room；11, liquid distribution trough；12, rectifying room；13, condenser；14, air pressure is pacified
Full valve；15, copper pipe b；16, temperature indicator；17, the first endless tube；18, the second endless tube；19, jet thrust；20, air inlet is responsible for；21,
Gas vent.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Embodiment
Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5 and Fig. 6 are please referred to, the utility model provides a kind of technical solution: a kind of rectifying point
From packed tower, including tower body 1, preheater 3, liquid distribution trough 11, condenser 13, heater 8 and it is fixed inside tower body 1
Discharge of steam part 9, heater 8 is connect with discharge of steam part 9 by pipeline, between discharge of steam part 9 and liquid distribution trough 11
It is provided with stripping room 10,11 upper surface of liquid distribution trough is to being provided with rectifying room 12,3 one side of preheater between 1 top of tower body
Upper end is provided with material liquid import 2, and another side lower end is connect with liquid distribution trough 11 by pipeline, and 3 inner bottom of preheater
End is provided with copper pipe b15, and lateral surface bottom end is provided with water pump 4, and the one end copper pipe b15 is connect with 4 water outlet of water pump, 1 inside of tower body
Face lower end is surrounded with heat dump 6, and copper pipe a7 is fixedly installed inside heat dump 6, and the one end copper pipe a7 and 4 water sucking mouth of water pump connect
It connects, the other end is connect with copper pipe b15 by pipeline, passes through heat dump by setting heat dump 6 and copper pipe a7, liquefied steam water
6 transfer heat to copper pipe a7, then are recycled to the copper pipe b15 in preheater 3 by water pump 4, will be entered by material liquid import 2 pre-
Material liquid in hot device 3 is preheated, and the rate that material liquid is fractionated in tower body 1 is accelerated, and reduces energy consumption.
In the present embodiment, it is preferred that discharge of steam part 9 includes the first endless tube 17 and the second endless tube 18, the first endless tube 17 with
Second endless tube 18 is connected by pipeline, and there are gaps between the first endless tube 17 and the second endless tube 18, pass through convenient for top fraction
Discharge of steam part 9 falls to tower bottom, and the first endless tube 17 and 18 lower end surface of the second endless tube be surrounded with it is multiple equally distributed
Jet thrust 19,19 lower end surface of jet thrust middle part are provided with air inlet supervisor 20, and lower end surface edge is surrounded with multiple gas vents 21,
By the way that gas vent 21 is arranged at 19 lower end surface edge of jet thrust, prevents the fraction of upper end from entering in jet thrust 19, lead to jet
First 19 are blocked.
In the present embodiment, it is preferred that it is come into full contact with for the ease of copper pipe a7 and heat dump 6, copper pipe a7 is spiral-shaped structure,
In order to make material liquid fully absorb the heat in copper pipe b15, copper pipe b15 is " S " type structure.
In the present embodiment, it is preferred that be fractionated for the ease of carrying out heating again to tower bottom fraction, 6 lower end of heat dump is set
It is equipped with tower bottom cone tank 5,5 bottom end of tower bottom cone tank is provided with discharge outlet, and heater 8 passes through pipeline and the discharge outlet air-tightness
Connection.
In the present embodiment, it is preferred that temperature is excessively high in order to prevent causes air pressure to rise, and influences the safety of equipment, preheater 3
Upper surface side is provided with air pressure relief valve 14, and middle part is provided with temperature indicator 16.
The working principle and process for using of the utility model:
It opens water pump 4 heat that heat dump 6 absorbs is sent in preheater 3, then preheating will be passed through to rectifying material liquid
Device 3 is preheated, and is passed through by liquid distribution trough 11 into tower.
3 one side upper end of preheater is provided with material liquid import 2, and another side lower end and liquid distribution trough 11 pass through pipeline
Connection, and 3 inner bottom of preheater is provided with copper pipe b15, lateral surface bottom end is provided with water pump 4, the one end copper pipe b15 and water pump 4
Water outlet connection, 1 medial surface lower end of tower body is surrounded with heat dump 6, copper pipe a7, copper pipe is fixedly installed inside heat dump 6
The one end a7 is connect with 4 water sucking mouth of water pump, and the other end is connect with copper pipe b15 by pipeline, by the way that heat dump 6 and copper pipe a7 is arranged,
Liquefied steam water transfers heat to copper pipe a7 by heat dump 6, then is recycled to the copper pipe b15 in preheater 3 by water pump 4,
The material liquid entered in preheater 3 by material liquid import 2 is preheated, the rate that material liquid is fractionated in tower body 1 is accelerated,
Reduce energy consumption.
Discharge of steam part 9 includes the first endless tube 17 and the second endless tube 18, and the first endless tube 17 and the second endless tube 18 pass through pipeline
Connection, there are gaps between the first endless tube 17 and the second endless tube 18, fall to tower by discharge of steam part 9 convenient for top fraction
Bottom, and the first endless tube 17 and 18 lower end surface of the second endless tube are surrounded with multiple equally distributed jet thrusts 19, under jet thrust 19
Air inlet supervisor 20 is provided in the middle part of end face, lower end surface edge is surrounded with multiple gas vents 21, by 19 lower end of jet thrust
Gas vent 21 is arranged in face edge, prevents the fraction of upper end from entering in jet thrust 19, and jet thrust 19 is caused to be blocked.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (5)
1. a kind of rectifying separates packed tower, including tower body (1), preheater (3), liquid distribution trough (11), condenser (13), heating
Device (8) and the discharge of steam part (9) for being fixed at the tower body (1) inside, the heater (8) and the discharge of steam part
(9) it is connected by pipeline, it is characterised in that: be provided with and mention between the discharge of steam part (9) and the liquid distribution trough (11)
It evaporates room (10), liquid distribution trough (11) upper surface is provided with rectifying room (12) between the tower body (1) top, described pre-
Hot device (3) one side upper end is provided with material liquid import (2), and another side lower end and the liquid distribution trough (11) pass through pipeline
Connection, and the preheater (3) inner bottom is provided with copper pipe b(15), lateral surface bottom end is provided with water pump (4), the copper pipe b
(15) one end is connect with the water pump (4) water outlet, and tower body (1) the medial surface lower end is surrounded with heat dump (6), described
Heat dump (6) is internally provided with copper pipe a(7), the copper pipe a(7) one end connect with the water pump (4) water sucking mouth, the other end with
The copper pipe b(15) it is connected by pipeline.
2. a kind of rectifying according to claim 1 separates packed tower, it is characterised in that: the discharge of steam part (9) includes
First endless tube (17) and the second endless tube (18), first endless tube (17) are connect with second endless tube (18) by pipeline, and
First endless tube (17) and second endless tube (18) lower end surface are surrounded with multiple equally distributed jet thrusts (19), institute
It states and is provided with air inlet supervisor (20) in the middle part of jet thrust (19) lower end surface, lower end surface edge is surrounded with multiple gas vents (21).
3. a kind of rectifying according to claim 1 separates packed tower, it is characterised in that: the copper pipe a(7) it is screw type knot
Structure, the copper pipe b(15) it is " S " type structure.
4. a kind of rectifying according to claim 1 separates packed tower, it is characterised in that: heat dump (6) the lower end setting
Have tower bottom cone tank (5), tower bottom cone tank (5) bottom end is provided with discharge outlet, and the heater (8) by pipeline and is somebody's turn to do
The connection of discharge outlet air-tightness.
5. a kind of rectifying according to claim 1 separates packed tower, it is characterised in that: preheater (3) upper surface one
Side is provided with air pressure relief valve (14), and middle part is provided with temperature indicator (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920028961.1U CN209378484U (en) | 2019-01-09 | 2019-01-09 | A kind of rectifying separation packed tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920028961.1U CN209378484U (en) | 2019-01-09 | 2019-01-09 | A kind of rectifying separation packed tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209378484U true CN209378484U (en) | 2019-09-13 |
Family
ID=67863873
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920028961.1U Expired - Fee Related CN209378484U (en) | 2019-01-09 | 2019-01-09 | A kind of rectifying separation packed tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209378484U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112011408A (en) * | 2020-09-10 | 2020-12-01 | 无锡科伦达化工热力装备有限公司 | High-efficient tower of hydrolysising |
-
2019
- 2019-01-09 CN CN201920028961.1U patent/CN209378484U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112011408A (en) * | 2020-09-10 | 2020-12-01 | 无锡科伦达化工热力装备有限公司 | High-efficient tower of hydrolysising |
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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: 20190913 Termination date: 20210109 |