CN206081708U - Board -like rectifying column of micropore column plate - Google Patents
Board -like rectifying column of micropore column plate Download PDFInfo
- Publication number
- CN206081708U CN206081708U CN201621077097.7U CN201621077097U CN206081708U CN 206081708 U CN206081708 U CN 206081708U CN 201621077097 U CN201621077097 U CN 201621077097U CN 206081708 U CN206081708 U CN 206081708U
- Authority
- CN
- China
- Prior art keywords
- tower
- tower section
- templates
- section
- column
- 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
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a board -like rectifying column of micropore column plate, including tower cauldron, first tower section, second tower section, third tower section, top of the tower, spacer, the cooperation of tower cauldron is installed on the skirt, and the bottom of tower cauldron is equipped with the raffinate export, is equipped with steam inlet, lower temperature meter connector, overdraft meter connector and a plurality of level gauge on the tower cauldron, tower cauldron, first tower section, second tower section, third tower section, top of the tower from the bottom up link to each other with the tower section flange in proper order, be equipped with down the feed inlet on the tower body of first tower section, first tower section, second tower section, third tower section three's tower body is inside to be equipped with a plurality of layers of column plate, and the main part of column plate is worked in coordination the erection joint by a S template, the 3rd S template and a plurality of the 2nd not unidimensional S template and is formed, and the welding has a baffle on the S template, be fixed with a plurality of spacers on the tower body inner wall of first tower section, second tower section, third tower section, the spacer links to each other with the S template side that corresponds.
Description
【Technical field】
This utility model is related to the technical field of rectifying column, the technology neck of particularly a kind of micropore column plate plate distillation column
Domain.
【Background technology】
Rectifying column is a kind of tower vapor-liquid contacting apparatus for carrying out rectification, and rectifying column mainly has two kinds of plate column and packed tower
Type, according to mode of operation continuous rectifying tower and batch fractionating tower can be divided into again.Because iris type rectifying column is for multicomponent point
From the tremendous economic advantage with special extract rectification with low energy consumption, low cost, cause countries in the world professional and technical personnel and scholar
Extensive concern.Iris type rectifying column will be allocated into the uprising gas of dividing plate tower bottom due to needing in dividing plate both sides, this
Individual apportioning cost affects product purity and energy consumption in distillation process, appropriate gas apportioning cost to reduce the energy of partitioned column
Consumption, can also be significantly increased the purity of rectification product.There is tower body and be relatively large in diameter in existing some plate distillation columns, structure
Complicated not easy to operate, energy is easy to run off, and it is relatively low that dividing plate quantity and number of openings cause to concentrate less the solution concentration for purifying out, processes
Efficiency is low, and energy consumption cost is high, the problems such as control effect is not good.
【Utility model content】
The purpose of this utility model is exactly to solve the problems of the prior art, proposes a kind of micropore column plate plate distillation column,
The control effect of rectifying column can be made good, the efficiency and quality for separating rectification is high, and energy consumption cost is low, good seal performance, column plate and
The material of rectification is separated needed for quickly can processing layer by layer more than the quantity of through hole, stable working is good.
For achieving the above object, the utility model proposes a kind of micropore column plate plate distillation column, including tower reactor, the first tower
Section, the second tower section, the 3rd tower section, tower top, spacer, the tower reactor coordinates on skirt, and the bottom of tower reactor is provided with residual liquid
Outlet, tower reactor is provided with steam inlet, lower temperature meter connector, lower pressure tapping and some liquidometers, the tower reactor, the first tower
Section, the second tower section, the 3rd tower section, tower top are connected with tower section flange successively from top to bottom, and the tower body of the first tower section is provided with
Lower charging aperture, if being provided with dried layer column plate, the master of column plate inside the first tower section, the second tower section, the tower body of the 3rd tower section three
Body is formed by connecting by the installation of working in coordination of a S templates, the 3rd S templates and some various sizes of 2nd S templates, a S types
Baffle plate is welded with plate, on the first tower section, the second tower section, the tower body inwall of the 3rd tower section some spacers are fixed with, it is fixed
Bit slice is connected with corresponding S templates side, and the second tower section is provided with thermometer joint and enterprising material mouth, and the described 3rd
Refluxing opening is offered on tower section, packing area is provided with the tower top, coordinated in packing area and filler support is installed, the tower top
Upper end is provided with the end socket of arc-shaped, and end socket is provided with temperature meter connector, upward pressure meter connector and gas outlet.
Preferably, being equipped with some symmetrical regarding on the tower reactor, the first tower section, the second tower section, the 3rd tower section
Mirror, the working condition being convenient for people in observing tower, it is ensured that good work efficiency and quality.
Preferably, the tower section flange respectively with tower reactor, the first tower section, the second tower section, the 3rd tower section, tower top tower body
Outer wall welding manner is connected, a S templates, the 3rd S templates, the 2nd S templates installation position in the neighbouring two-layer column plate
Put contrary so that the sound construction of rectifying column, liquefied gass can be carried out column plate with separation rectification process layer by layer, improve
Separate the treatment effeciency and quality of rectification.
Preferably, the 3rd S templates and the 2nd S templates are provided with and are equipped with some through holes, on every layer of column plate
The 2nd S template quantity be 3 and three piece of the 2nd S template on through-hole diameter it is different, various sizes of 2nd S templates cause for
Gas liquid carries out separating treatment step by step, it is ensured that detached efficiency and quality are high.
The beneficial effects of the utility model：This utility model by end socket by being provided with upper temperature meter connector, upward pressure table
Joint, the second tower section is provided with thermometer joint, and tower reactor is provided with lower temperature meter connector, lower pressure tapping and some liquid levels
Meter so that people can in real time grasp the data parameters in rectifying column, so that people adjust in time according to demand relevant parameter, from
And ensureing that material rectification is detached is efficiently carried out；If will be provided with inside the first tower section, the second tower section, the tower body of the 3rd tower section three
Dried layer column plate, the main body of column plate is worked in coordination connection by a S templates, the 3rd S templates and some various sizes of 2nd S templates
Form, baffle plate is welded with a S templates, it is some fixed to be fixed with the first tower section, the second tower section, the tower body inwall of the 3rd tower section
Bit slice, spacer is connected with corresponding S templates side, and such mounting means ensure that the sound construction resistance to erosion of column plate
And resistance to compression, certain liquid layer can be accumulated on column plate conveniently carries out gas-liquid exchange raising separation rectification efficiency, can progressively to gas
Body fluid body carries out separating treatment, and liquid makes the separation efficacy exertion of tower to maximum with the defluent route of S types；By the 3rd tower section
Refluxing opening is provided with so that the produced quantity of rectifying column, capacity of returns are precisely controlled with optimum mode, so that the energy of tower
Consumption, material consumption are minimized, and separate effect optimal；The bottom of tower reactor is provided with into residual liquid outlet, end socket is provided with gas outlet so that
Toward dirty, toward rising, gas-liquid can be exchanged effectively gas liquid, and separation efficiency is high；To set on 3rd S templates and the 2nd S templates
It is equipped with some through holes so that the flow rate of gas liquid is good, accelerates to separate；The control effect of the rectifying column is good, separates essence
The efficiency for evaporating and quality are high, and energy consumption cost is low, good seal performance, needed for quickly can processing layer by layer more than the quantity of column plate and through hole
The material of rectification is separated, stable working is good.
Feature of the present utility model and advantage will combine accompanying drawing and be described in detail by embodiment.
【Description of the drawings】
Fig. 1 is a kind of schematic diagram of micropore column plate plate distillation column of this utility model；
Fig. 2 is a kind of schematic internal view of micropore column plate plate distillation column of this utility model；
Fig. 3 is a kind of top view of micropore column plate plate distillation column of this utility model；
Fig. 4 is a kind of tower reactor schematic diagram of micropore column plate plate distillation column of this utility model；
Fig. 5 is a kind of the first tower section schematic diagram of micropore column plate plate distillation column of this utility model；
Fig. 6 is a kind of the first tower section top view of micropore column plate plate distillation column of this utility model；
Fig. 7 is a kind of the second tower section schematic diagram of micropore column plate plate distillation column of this utility model；
Fig. 8 is a kind of the 3rd tower section schematic diagram of micropore column plate plate distillation column of this utility model；
Fig. 9 is a kind of A portions enlarged diagram of micropore column plate plate distillation column of this utility model；
Figure 10 is a kind of tower top schematic diagram of micropore column plate plate distillation column of this utility model；
Figure 11 is a kind of partial schematic diagram of micropore column plate plate distillation column of this utility model；
Figure 12 is a kind of the 2nd S template front views of micropore column plate plate distillation column of this utility model；
Figure 13 is a kind of the 2nd S template top views of micropore column plate plate distillation column of this utility model；
Figure 14 is an a kind of S template front views of micropore column plate plate distillation column of this utility model；
Figure 15 is an a kind of S template top views of micropore column plate plate distillation column of this utility model；
Figure 16 is a kind of the 3rd S template front views of micropore column plate plate distillation column of this utility model；
Figure 17 is a kind of the 3rd S template top views of micropore column plate plate distillation column of this utility model.
In figure：1- tower reactors, 2- the first tower sections, 3- the second tower sections, the tower sections of 4- the 3rd, 5- tower tops, 6- spacers, 7- visors,
Temperature meter connector, 15- are pushed under 8- tower section flanges, 10- skirts, the outlet of 11- residual liquids, 12- liquidometers, 13- steam inlets, 14-
Charging aperture, 31- thermometer joints, the enterprising material mouths of 32-, 41- refluxing openings, 51- filler supports, 52- fillers under power meter connector, 21-
Area, 53- end sockets, the upper temperature meter connectors of 54-, 55- upward pressure meter connectors, 56- gas outlets, the S templates of 61- the, 62- baffle plates,
The S templates of 63- the 2nd, the S templates of 64- the 3rd.
【Specific embodiment】
Refering to Fig. 1 to Figure 17, a kind of micropore column plate plate distillation column of this utility model, including tower reactor 1, the first tower section 2,
Two tower sections 3, the 3rd tower section 4, tower top 5, spacer 6, the tower reactor 1 coordinates on skirt 10, and the bottom of tower reactor 1 is provided with residual
Liquid outlet 11, tower reactor 1 is provided with steam inlet 13, lower temperature meter connector 14, lower pressure tapping 15 and some liquidometers 12, institute
State tower reactor 1, the first tower section 2, the second tower section 3, the 3rd tower section 4, tower top 5 to be connected with tower section flange 8 successively from top to bottom, described the
The tower body of one tower section 2 is provided with lower charging aperture 21, inside the first tower section 2, the second tower section 3, tower body of the three of the 3rd tower section 4
If being provided with dried layer column plate, the main body of column plate is by a S templates 61, the 3rd S templates 64 and some various sizes of 2nd S templates 63
Installation of working in coordination is formed by connecting, and baffle plate 62, the first tower section 2, the second tower section 3, the 3rd tower are welded with a S templates 61
Some spacers 6 are fixed with the tower body inwall of section 4, spacer 6 is connected with the corresponding side of a S templates 61, described second
Tower section 3 is provided with thermometer joint 31 and enterprising material mouth 32, refluxing opening 41 is offered on the 3rd tower section 4, in the tower top 5
It is provided with to coordinate in packing area 52, packing area 52 and filler support 51 is installed, the upper end of the tower top 5 is provided with the end socket of arc-shaped
53, end socket 53 is provided with temperature meter connector 54, upward pressure meter connector 55 and gas outlet 56, the tower reactor 1, the first tower section 2,
Be equipped with some symmetrical visors 7 on second tower section 3, the 3rd tower section 4, the tower section flange 8 respectively with tower reactor 1, first
Tower section 2, the second tower section 3, the 3rd tower section 4, the tower body outer wall welding manner of tower top 5 are connected, the neighbouring two-layer column plate
In a S templates 61, the 3rd S templates 64, installation site of the 2nd S templates 63 conversely, the 3rd S templates 64 and the 2nd S templates
63 are provided with and are equipped with some through holes, and the quantity of the 2nd S templates 63 on every layer of column plate is on 3 and three piece of the 2nd S template 63
Through-hole diameter it is different.
Utility model works process：
A kind of micropore column plate plate distillation column of this utility model in the course of the work, (is with Separate System of Water-jet during operation
Example), gas is entered from steam inlet 13, down charging in charging aperture 21 and enterprising material mouth 32, liquid under gravity, from upper
And under flow successively through each layer column plate inside the 3rd tower section 4, the second tower section 3, the first tower section 2, export from the residual liquid of the bottom of tower reactor 1
11 discharge, and steam gas are sequentially passed through from bottom to top in the first tower section 2, the second tower section 3, the 3rd tower section 4 under pressure differential promotion
Each layer column plate in portion, the gas outlet 56 from tower top 5 discharges, and wherein people can observe each several part work feelings from visor 7
Condition, adjusts the physical environmental factors such as pressure, temperature and feeding quantity and gas injection rate in tower, due to a S according to liquidometer 12
Template 61, the 3rd S templates 64, the installation connected mode between the 2nd S templates 63 and baffle plate 62 cause to be kept on every layer of column plate
The liquid layer of certain depth, and the through hole on the 3rd S templates 64, the 2nd S templates 63 then facilitates the flowing of liquid and gas, steam
Gas constantly shifts difficult volatile component in steam in the liquid layer being distributed on column plate through after through hole, carries out the contact of phase border and passes
Matter, makes volatile material it is discharged from gas outlet 56 in the presence of temperature, pressure, liquid in order from it is lower under successively
Through hole is flow through, volatile components are constantly shifted in steam in period liquid, finally discharged from residual liquid outlet 11.
A kind of micropore column plate plate distillation column of this utility model, by by end socket 53 be provided with upper temperature meter connector 54, on
Pressure tapping 55, the second tower section 3 is provided with thermometer joint 31, and tower reactor 1 is provided with lower temperature meter connector 14, lower pressure gauge and connects
15 and some liquidometers 12 so that people can in real time grasp the data parameters in rectifying column, so as to people according to demand and
When adjust relevant parameter, efficiently carry out so as to ensure that material rectification is detached；By the first tower section 2, the second tower section 3, the 3rd tower section 4
If being provided with dried layer column plate inside the tower body of three, the main body of column plate is by a S templates 61, the 3rd S templates 64 and some different chis
The 2nd very little S templates 63 are worked in coordination and are formed by connecting, and baffle plate 62, the first tower section 2, the second tower section are welded with a S templates 61
3rd, some spacers 6 are fixed with the tower body inwall of the 3rd tower section 4, spacer 6 is connected with the corresponding side of a S templates 61,
Such mounting means ensure that the sound construction resistance to erosion of column plate and resistance to compression, certain liquid layer can be accumulated on column plate and is conveniently entered
Circulation of qi promoting liquid is exchanged to improve and separates rectification efficiency, and separating treatment progressively can be carried out to gas liquid, and liquid is defluent with S types
Route makes the separation efficacy exertion of tower to maximum；3rd tower section 4 is provided with into refluxing opening 41 so that the produced quantity of rectifying column, return
Flow is precisely controlled with optimum mode, so that the energy consumption of tower, material consumption are minimized, separates effect optimal；By tower reactor 1
Bottom be provided with residual liquid outlet 11, end socket 53 is provided with gas outlet 56 so that toward dirty, toward rising, gas-liquid can for gas for liquid
Effectively to exchange, separation efficiency is high；3rd S templates 64 and the 2nd S templates 63 are provided with and are equipped with some through holes so that gas
The flow rate of liquid is good, accelerates to separate；The control effect of the rectifying column is good, and the efficiency and quality for separating rectification is high, energy consumption cost
Low, good seal performance separates the material of rectification, stable working needed for quickly can processing layer by layer more than the quantity of column plate and through hole
It is good.
Above-described embodiment be to explanation of the present utility model, be not to restriction of the present utility model, it is any new to this practicality
Scheme after type simple transformation belongs to protection domain of the present utility model.
Claims (4)
1. a kind of micropore column plate plate distillation column, it is characterised in that：Including tower reactor (1), the first tower section (2), the second tower section (3),
3rd tower section (4), tower top (5), spacer (6), the tower reactor (1) coordinates on skirt (10), and the bottom of tower reactor (1) sets
Have residual liquid export (11), tower reactor (1) be provided with steam inlet (13), lower temperature meter connector (14), lower pressure tapping (15) and
Some liquidometers (12), the tower reactor (1), the first tower section (2), the second tower section (3), the 3rd tower section (4), tower top (5) from it is lower to
On successively with tower section flange (8) be connected, the tower body of the first tower section (2) is provided with lower charging aperture (21), the first tower section
(2), if being provided with dried layer column plate inside the tower body of three, the main body of column plate is by a S templates for the second tower section (3), the 3rd tower section (4)
(61), the 3rd S templates (64) and some various sizes of 2nd S templates (63) installation of working in coordination is formed by connecting, a S templates
(61) it is welded with baffle plate (62) on, it is the first tower section (2), the second tower section (3), fixed on the tower body inwall of the 3rd tower section (4)
There are some spacers (6), spacer (6) is connected with a corresponding S templates (61) side, and the second tower section (3) is provided with
Thermometer joint (31) and enterprising material mouth (32), offer in refluxing opening (41), the tower top (5) on the 3rd tower section (4)
It is provided with to coordinate in packing area (52), packing area (52) and filler support (51) is installed, the upper end of the tower top (5) is provided with arc-shaped
End socket (53), end socket (53) is provided with temperature meter connector (54), upward pressure meter connector (55) and gas outlet (56).
2. a kind of micropore column plate plate distillation column as claimed in claim 1, it is characterised in that：The tower reactor (1), the first tower section
(2), some symmetrical visors (7) are equipped with the second tower section (3), the 3rd tower section (4).
3. a kind of micropore column plate plate distillation column as claimed in claim 1, it is characterised in that：The tower section flange (8) is respectively
It is connected with the tower body outer wall welding manner of tower reactor (1), the first tower section (2), the second tower section (3), the 3rd tower section (4), tower top (5),
A S templates (61), the 3rd S templates (64), the 2nd S templates (63) installation site phase in the neighbouring two-layer column plate
Instead.
4. a kind of micropore column plate plate distillation column as claimed in claim 1, it is characterised in that：The 3rd S templates (64) and
2nd S templates (63) are provided with and are equipped with some through holes, and the 2nd S templates (63) quantity on every layer of column plate is 3 and three pieces
Through-hole diameter on 2nd S templates (63) is different.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621077097.7U CN206081708U (en) | 2016-09-26 | 2016-09-26 | Board -like rectifying column of micropore column plate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621077097.7U CN206081708U (en) | 2016-09-26 | 2016-09-26 | Board -like rectifying column of micropore column plate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206081708U true CN206081708U (en) | 2017-04-12 |
Family
ID=58479431
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621077097.7U Active CN206081708U (en) | 2016-09-26 | 2016-09-26 | Board -like rectifying column of micropore column plate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206081708U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110215729A (en) * | 2018-03-01 | 2019-09-10 | 无锡科伦达化工热力装备有限公司 | A kind of plate distillation column |
-
2016
- 2016-09-26 CN CN201621077097.7U patent/CN206081708U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110215729A (en) * | 2018-03-01 | 2019-09-10 | 无锡科伦达化工热力装备有限公司 | A kind of plate distillation column |
| CN110215729B (en) * | 2018-03-01 | 2021-06-29 | 无锡科伦达化工热力装备有限公司 | Plate-type rectifying tower |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204224560U (en) | Natural gas conditioning depickling sledge | |
| CN209865355U (en) | Chemical industry is with having filtered high-efficient rectifying column of pressurization | |
| CN209835629U (en) | Dilute sulfuric acid treatment device in production of hydrogen fluoride prepared from fluosilicic acid | |
| CN206081708U (en) | Board -like rectifying column of micropore column plate | |
| CN204824783U (en) | Natural gas deacidification purifier | |
| CN202620940U (en) | Complete device for removing aluminum chloride heavy metal impurities in cold hydrogenation tail gas | |
| CN104083889B (en) | High-efficient energy-saving alcohol recovery tower | |
| CN203200237U (en) | Physical deacidifying tower of vegetable oil with high acid value | |
| CN206642392U (en) | A kind of triphenyl phosphite rectifying column | |
| CN203479062U (en) | Flue gas afterheat and water recycling device | |
| CN109126167B (en) | EO concentration tower structure | |
| CN210096971U (en) | Rectification equipment capable of separating three components simultaneously | |
| CN101913609A (en) | Method and device for removing impurities from trichlorosilane mixed gas | |
| CN112899019B (en) | Full-center gravity flow oil gas water treatment device | |
| CN202052457U (en) | Novel low-pressure carbon dioxide regeneration tower | |
| CN203540100U (en) | Dimethyl sulfate rectifying tower | |
| CN202342932U (en) | Tower plate filler type rectifying tower | |
| CN209005247U (en) | A kind of Chinese patent drug production alcohol high efficiente callback tower | |
| CN207203801U (en) | A kind of osmium, ruthenium gas absorbing device | |
| CN207371134U (en) | A kind of gas stripping type reboiler and absorption plant | |
| CN207463199U (en) | A kind of packed tower with dredging | |
| CN207102226U (en) | A kind of no-arbitrary pricing Tower for purifying waste gas | |
| CN201610390U (en) | Water feeding device of integrated oxygen remover | |
| CN206934783U (en) | A kind of trichlorosilane rectifying column removes light system | |
| CN204824188U (en) | Silane rectifying column |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |