CN208611833U - Multi-stage distillation equipment - Google Patents
Multi-stage distillation equipment Download PDFInfo
- Publication number
- CN208611833U CN208611833U CN201821044725.0U CN201821044725U CN208611833U CN 208611833 U CN208611833 U CN 208611833U CN 201821044725 U CN201821044725 U CN 201821044725U CN 208611833 U CN208611833 U CN 208611833U
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- CN
- China
- Prior art keywords
- accumulation
- heat
- filler
- distillery
- distillation
- 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.)
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- 238000004821 distillation Methods 0.000 title claims abstract description 22
- 238000009825 accumulation Methods 0.000 claims abstract description 24
- 239000000463 material Substances 0.000 claims abstract description 22
- 239000000945 filler Substances 0.000 claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims abstract description 13
- 238000003860 storage Methods 0.000 claims abstract description 8
- 239000007921 spray Substances 0.000 claims abstract description 6
- 238000005485 electric heating Methods 0.000 claims abstract description 5
- 238000005192 partition Methods 0.000 claims abstract description 5
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 6
- 239000011449 brick Substances 0.000 claims description 3
- 239000000395 magnesium oxide Substances 0.000 claims description 3
- 238000002309 gasification Methods 0.000 abstract description 5
- 239000002245 particle Substances 0.000 abstract description 2
- 238000009834 vaporization Methods 0.000 abstract description 2
- 230000008016 vaporization Effects 0.000 abstract description 2
- 238000005457 optimization Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000011344 liquid material Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to multi-stage distillation equipments.Enclosure interior is separated into multiple distilleries by partition, and discharge nozzle connects condenser, and condenser material outlet connects storage tank, and step-like accumulation of heat is equipped with inside distillery and heats filler, accumulation of heat heats and is equipped with electric heating wire inside filler, and distillery bottom is equipped with drain pipe.Material is ejected on accumulation of heat heating filler from the material spray head of discharge nozzle with misty little particle, and material is heated gasification distillation on accumulation of heat heating filler, and step-like accumulation of heat heating filler extends material heating stroke, promotes material and be sufficiently vaporized distillation.The utility model is distilled suitable for continuity feed vaporization, improves distillation efficiency.
Description
Technical field
The utility model relates to chemical plant installations technical fields, and in particular to multi-stage distillation equipment.
Background technique
In organic chemistry production, distilation mostly is carried out using destilling tower.Tower is many kinds of, and destilling tower is to be steamed
A kind of tower gas-liquid contact apparatus evaporated.There are plate column and two kinds of main Types of packed tower.Plate column is compared with packed tower
The problem of a complexity, there are many factor being related to, and when type selecting is considered as material properties, operating condition, the performance of tower, Yi Jita
Manufacture, installation, operating and maintenance of equipment etc..Destilling tower principle of distillation is by liquid mixture partial gasification, and utilization is wherein each
The different characteristic of component volatilization degree realizes separation.Tower reactor is liquid, overhead gas.Due to material properties and distill tower-shaped
The limitation of shape keeps distilation efficiency limited.
Summary of the invention
Purpose of the utility model is to solve the above problems and provide a kind of multi-stage distillation equipment, distillation efficiency is high.
To solve the above-mentioned problems, the technical solution adopted in the utility model is as follows:
Multi-stage distillation equipment, which is characterized in that be separated into including horizontal square shell 1, inside shell 1 by partition 2 multiple
Distillery 3, feed pipe 31 and discharge nozzle 32 are equipped at the top of distillery 3, and 31 end of feed pipe is equipped with material spray head 35, discharge nozzle 32
Condenser 4 is connected, condenser material outlet connects storage tank 5, and storage tank 5 connects vacuum plant 6, is equipped with rank inside distillery 3
Filler 33 is heated in trapezoidal accumulation of heat, and accumulation of heat heats and is equipped with electric heating wire 34 inside filler 33, and 3 bottom of distillery is equipped with drain pipe
36, drain pipe 36 is equipped with valve.
Optimization, the accumulation of heat heating filler is accumulation of heat magnesia brick.
Optimization, feed pipe 31 connect warmup heater 7.
Compared with prior art, the utility model advantageous effects are as follows:
Material is ejected on accumulation of heat heating filler from the material spray head of discharge nozzle with misty little particle, heats filler in accumulation of heat
Upper material is heated gasification distillation, and unvaporized liquid material is continued traveling downwardly along accumulation of heat heating filler and is heated, further
Gasification distillation.Step-like accumulation of heat heating filler extends material heating stroke, promotes material and is sufficiently vaporized distillation, non-gas
The liquid material of change is distilled from the drain pipe outlet of bottom without circulation.
The utility model is distilled suitable for continuity feed vaporization, improves distillation efficiency.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is multi-stage distillation equipment structural schematic diagram described in the utility model；
Description of symbols: filler-is heated in shell -1, partition -2, distillery -3, feed pipe -31, discharge nozzle -32, accumulation of heat
33, electric heating wire -34, material spray head -35, drain pipe -36, condenser -4, storage tank -5, vacuum plant -6, warmup heater -
7。
Specific embodiment
The preferred embodiment of the utility model is described in detail with reference to the accompanying drawing, so that the advantages of the utility model
It can be easier to be readily appreciated by one skilled in the art with feature, to make the protection scope of the utility model apparent clear
Define.
Refering to shown in Figure of description 1, multi-stage distillation equipment, which is characterized in that including horizontal square shell 1, in shell 1
Portion is separated into multiple distilleries 3 by partition 2, is equipped with feed pipe 31 and discharge nozzle 32 at the top of distillery 3,31 end of feed pipe is equipped with
Material spray head 35, discharge nozzle 32 connect condenser 4, and condenser material outlet connects storage tank 5, and storage tank 5 connects vacuum plant
6, it is equipped with step-like accumulation of heat inside distillery 3 and heats filler 33, accumulation of heat heats and is equipped with electric heating wire 34 inside filler 33, distillation
3 bottom of room is equipped with drain pipe 36, and drain pipe 36 is equipped with valve.
Optimization, the accumulation of heat heating filler is accumulation of heat magnesia brick.In order to make full use of waste heat, this specific embodiment selects accumulation of heat
Heat filler.
Optimization, feed pipe 31 connect warmup heater 7.Material enter distillery before be preheated, the material after preheating with
Accumulation of heat heats filler device contact and sufficiently carries out heat exchange, accelerates gasification distillation efficiency.
Basic principles, main features, and advantages of the present invention has been shown and described above.Current row
The technical staff of industry is it should be appreciated that the present utility model is not limited to the above embodiments, retouching in above embodiments and description
The preference of only the utility model is stated, the utility model is not limited by above-mentioned preference, is not departing from the utility model
Under the premise of spirit and scope, the utility model can also have various changes and modifications, these changes and improvements both fall within practical
In novel claimed range.
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 (3)
1. multi-stage distillation equipment, which is characterized in that including horizontal square shell (1), be separated into inside shell (1) by partition (2)
Multiple distilleries (3), distillery (3) top are equipped with feed pipe (31) and discharge nozzle (32), and feed pipe (31) end is equipped with material
Spray head (35), discharge nozzle (32) connect condenser (4), and condenser material outlet connects storage tank (5), and storage tank (5) connection is true
Empty device (6), distillery (3) is internal to be equipped with step-like accumulation of heat heating filler (33), is equipped with inside accumulation of heat heating filler (33)
Electric heating wire (34), distillery (3) bottom are equipped with drain pipe (36), and drain pipe (36) is equipped with valve.
2. multi-stage distillation equipment according to claim 1, which is characterized in that the accumulation of heat heating filler is accumulation of heat magnesia brick.
3. multi-stage distillation equipment according to claim 1, which is characterized in that feed pipe (31) connects warmup heater (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821044725.0U CN208611833U (en) | 2018-07-03 | 2018-07-03 | Multi-stage distillation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821044725.0U CN208611833U (en) | 2018-07-03 | 2018-07-03 | Multi-stage distillation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208611833U true CN208611833U (en) | 2019-03-19 |
Family
ID=65704555
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821044725.0U Active CN208611833U (en) | 2018-07-03 | 2018-07-03 | Multi-stage distillation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208611833U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110124357A (en) * | 2019-05-13 | 2019-08-16 | 江苏九九久科技有限公司 | Volatile impurity removes easy device in fluid |
| CN111689636A (en) * | 2020-07-10 | 2020-09-22 | 新昌县海博科技股份有限公司 | Sewage treatment regenerator and sewage treatment process |
-
2018
- 2018-07-03 CN CN201821044725.0U patent/CN208611833U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110124357A (en) * | 2019-05-13 | 2019-08-16 | 江苏九九久科技有限公司 | Volatile impurity removes easy device in fluid |
| CN111689636A (en) * | 2020-07-10 | 2020-09-22 | 新昌县海博科技股份有限公司 | Sewage treatment regenerator and sewage treatment process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 113000 Zhangdian Street, Dongzhou District, Fushun City, Liaoning Province Patentee after: Jinjiuqi (Fushun) Pharmaceutical Co.,Ltd. Address before: 113000 Zhangdian Street, Dongzhou District, Fushun City, Liaoning Province Patentee before: FUSHUN DAHENG CHEMICAL Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Multiflavor steamer Effective date of registration: 20201021 Granted publication date: 20190319 Pledgee: Shenyang Shengjing Financing Guarantee Co.,Ltd. Pledgor: Jinjiuqi (Fushun) Pharmaceutical Co.,Ltd. Registration number: Y2020210000057 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20210401 Granted publication date: 20190319 Pledgee: Shenyang Shengjing Financing Guarantee Co.,Ltd. Pledgor: Jinjiuqi (Fushun) Pharmaceutical Co.,Ltd. Registration number: Y2020210000057 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Multistage distillation unit Effective date of registration: 20210409 Granted publication date: 20190319 Pledgee: Shenyang Shengjing Financing Guarantee Co.,Ltd. Pledgor: Jinjiuqi (Fushun) Pharmaceutical Co.,Ltd. Registration number: Y2021210000015 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20220714 Granted publication date: 20190319 Pledgee: Shenyang Shengjing Financing Guarantee Co.,Ltd. Pledgor: Jinjiuqi (Fushun) Pharmaceutical Co.,Ltd. Registration number: Y2021210000015 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Multistage distillation unit Effective date of registration: 20230320 Granted publication date: 20190319 Pledgee: Shenyang Branch of Dandong Bank Co.,Ltd. Pledgor: Jinjiuqi (Fushun) Pharmaceutical Co.,Ltd. Registration number: Y2023210000043 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |