CN208177003U - Heat-preserving and energy-saving distillation device - Google Patents
Heat-preserving and energy-saving distillation device Download PDFInfo
- Publication number
- CN208177003U CN208177003U CN201820456337.7U CN201820456337U CN208177003U CN 208177003 U CN208177003 U CN 208177003U CN 201820456337 U CN201820456337 U CN 201820456337U CN 208177003 U CN208177003 U CN 208177003U
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- CN
- China
- Prior art keywords
- acquisition
- pipeline
- casing
- condenser
- tank
- Prior art date
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- 238000004821 distillation Methods 0.000 title abstract description 9
- 238000004321 preservation Methods 0.000 claims abstract description 13
- 238000010992 reflux Methods 0.000 claims description 16
- 239000000498 cooling water Substances 0.000 claims description 7
- 230000003020 moisturizing effect Effects 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 5
- 238000002425 crystallisation Methods 0.000 abstract description 6
- 230000008025 crystallization Effects 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 1
- -1 biology Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a heat preservation and energy saving distillation plant, including distillation column, condenser and collection tank, distillation column and condenser between the intercommunication have steam conduit and return line, the intercommunication has the collection pipeline between condenser and the collection tank, return line and collection pipeline's periphery all be equipped with the sleeve pipe, the collection tank is equipped with outward and presss from both sides the cover, the condenser top is equipped with the steam outlet pipeline, the steam outlet pipeline respectively with the sleeve pipe of return line, the sleeve pipe intercommunication of collection pipeline, the sleeve pipe of collection pipeline and the cover intercommunication that presss from both sides of collection tank. The utility model discloses can avoid the crystallization to block up, reduce energy consumption and cost, raise the efficiency.
Description
Technical field
The utility model relates to distillation technique field, specifically a kind of heat preservation energy-saving distilling apparatus.
Background technique
Distillation is a kind of separating technology, is widely used in the industries such as chemical industry, petroleum, biology, medicine, pesticide, food, former
Reason is the boiling point difference using different material, separating treatment is carried out to the predetermined substance in mixture, to obtain certain substance
High-purity component, or isolate it is some do not need, the technical process of harmful substance.Distillation mainly includes evaporating and condensing two
Kind unit operation, in condensation phase, is condensed, at normal temperature due to some products by steam of the recirculated cooling water to evaporation
It is easy crystallization, is blocked in after crystallization in acquisition tank or collection tube, influences postorder distillation work, but also need a large amount of manpower
It is dredged, distillation work inefficiency.
Summary of the invention
The technical problem to be solved by the utility model is to provide one kind to avoid Crystallization Plugging, reduces energy consumption and cost, mentions
Efficient heat preservation energy-saving distilling apparatus.
The technical scheme adopted by the utility model is providing a kind of heat preservation energy-saving distilling apparatus, including destilling tower, condensation
Device and acquisition tank, are communicated with jet chimney and reflux line between the destilling tower and condenser, condenser and acquisition tank it
Between be communicated with acquisition pipeline, the periphery of the reflux line and acquisition pipeline is equipped with casing, and acquisition tank is externally provided with collet, cold
Be equipped with steam (vapor) outlet pipeline at the top of condenser, the steam (vapor) outlet pipeline respectively with the casing of reflux line, acquire the set of pipeline
Pipe connection, the casing for acquiring pipeline are connected to the collet of acquisition tank.
The casing of the reflux line is connected to the casing of acquisition pipeline by pipeline I.
The acquisition pipe outlet connection is connected to two acquisitions there are two lateral, two acquisition laterals are acquired
Tank, two acquisition lateral peripheries are respectively provided with casing, and the casing of two acquisition laterals passes through pipeline II and acquisition respectively
The collet of tank is connected to.
The inlet and outlet of the recirculated cooling water of the condenser are equipped with control valve, and recirculated cooling water entrance adds moisturizing
Control valve and moisturizing import is arranged in import, can be selected when distilling different products according to the temperature of product condensation different
Condensed water.
After using the above structure, the utility model heat preservation energy-saving distilling apparatus can pass through the steaming of acquisition condensation process generation
Vapour is used to carry out Heat preservation to the product of easy crystallization, avoids the problem that line clogging caused by crystallization, improves working efficiency；
The heat that heating heat acquisition system itself collected generates does not need the external additional energy, makes full use of energy consumption, and
It can reduce energy consumption and production costs.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model heat preservation energy-saving distilling apparatus.
In figure, 1, destilling tower, 2, jet chimney, 3, condenser, 4, steam (vapor) outlet pipeline, 5, control valve, 6, moisturizing into
Mouthful, 7, reflux line, 8, acquisition pipeline, 8.1, acquisition lateral, 9, acquisition tank, 9.1, collet, 10, casing, 11, pipeline I,
12, pipeline II.
Specific embodiment
The utility model is described in detail below in conjunction with drawings and examples.
As shown in Figure 1, the utility model heat preservation energy-saving distilling apparatus, including destilling tower 1, condenser 3 and acquisition tank 9, it steams
It evaporates and is communicated with jet chimney 2 and reflux line 7 between tower 1 and condenser 3.Collection tube is communicated between condenser 3 and acquisition tank 9
Road 8,2 one end of jet chimney are connected to 1 top of destilling tower, and 2 other end of jet chimney is connected to 3 top of condenser, reflux line 7
One end is connected to 3 bottom of condenser, and the other end is connected to 1 middle part of destilling tower；Acquisition 8 one end of pipeline is connected to 3 bottom of condenser,
The other end is connected to 9 top of acquisition tank, and reflux line 7 and acquisition 8 periphery of pipeline are equipped with casing 10, and acquisition tank 9 is externally provided with folder
Set 9.1, i.e., 10 internal diameter of casing be greater than reflux line 7 and acquisition 8 outer diameter of pipeline, casing 10 and acquisition pipeline 8 between, 10 and of casing
There is space between reflux line 7 and between collet 9.1 and acquisition tank 9, is equipped with steam (vapor) outlet pipeline 4, steam at the top of condenser 3
Outlet conduit 4 is connected to the casing 10 of the casing 10 of reflux line 7, acquisition pipeline 8 respectively, is acquired the casing 10 of pipeline 8 and is adopted
The collet 9.1 for collecting tank 9 is connected to.
In the specific implementation, the casing 10 of reflux line 7 and the casing 10 of acquisition pipeline 8 pass through pipeline I to the utility model
11 connections；It acquires 8 outlet of pipeline and is connected to two acquisitions there are two lateral 8.1, two acquisition laterals 8.1 are acquired
Tank 9, two 8.1 peripheries of acquisition lateral are respectively provided with casing, and the casing 10 of two acquisition laterals 8.1 passes through pipeline respectively
II 12 are connected to the collet 9.1 of acquisition tank 9.The inlet and outlet of the recirculated cooling water of condenser 3 are equipped with control valve 5, recycle cold
But moisturizing import 6 is added at water inlet.
When specifically used, the steam that destilling tower 1 generates passes through cold after the entrance condenser 3 of jet chimney 2 the utility model
Solidifying, the heat released heats the water in condenser 3, generates steam, and the steam of generation goes out from the steam at 3 top of condenser
Mouthful pipeline, which comes out, to be entered reflux line 7 and acquires the casing of pipeline 8 and be communicated in the collet of acquisition tank 9, and acquisition is made
Material achievees the purpose that heating and thermal insulation, and according to the characteristic of distillage, selection is intake from moisturizing import or circulating cooling water inlet
It is condensed, preferably different products effectively can be controlled.
Claims (4)
1. a kind of heat preservation energy-saving distilling apparatus, including destilling tower, condenser and acquisition tank, between the destilling tower and condenser
It is communicated with jet chimney and reflux line, is communicated with acquisition pipeline between condenser and acquisition tank, it is characterised in that: described returns
The periphery of flow tube road and acquisition pipeline is equipped with casing, and acquisition tank is externally provided with collet, and condenser overhead is equipped with steam (vapor) outlet pipeline,
The steam (vapor) outlet pipeline is connected to the casing of the casing of reflux line, acquisition pipeline respectively, is acquired the casing of pipeline and is adopted
Collect the collet connection of tank.
2. heat preservation energy-saving distilling apparatus according to claim 1, it is characterised in that: the casing of the reflux line and acquisition
The casing of pipeline is connected to by pipeline I.
3. heat preservation energy-saving distilling apparatus according to claim 2, it is characterised in that: the acquisition pipe outlet is communicated with
Two acquisition laterals, two acquisition laterals are connected to two acquisition tanks, and two acquisition lateral peripheries are respectively provided with set
Pipe, the casing of two acquisition laterals pass through pipeline II respectively and are connected to the collet for acquiring tank.
4. heat preservation energy-saving distilling apparatus according to claim 1, it is characterised in that: the recirculated cooling water of the condenser
Inlet and outlet are equipped with control valve, and recirculated cooling water entrance adds moisturizing import.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820456337.7U CN208177003U (en) | 2018-04-03 | 2018-04-03 | Heat-preserving and energy-saving distillation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820456337.7U CN208177003U (en) | 2018-04-03 | 2018-04-03 | Heat-preserving and energy-saving distillation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208177003U true CN208177003U (en) | 2018-12-04 |
Family
ID=64435790
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820456337.7U Active CN208177003U (en) | 2018-04-03 | 2018-04-03 | Heat-preserving and energy-saving distillation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208177003U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110384943A (en) * | 2019-08-28 | 2019-10-29 | 深圳市冠融辰环保科技有限公司 | A kind of multiple-effect vacuum evaporator high temperature goes out the salt preventing clogging up device out of salt effect |
-
2018
- 2018-04-03 CN CN201820456337.7U patent/CN208177003U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110384943A (en) * | 2019-08-28 | 2019-10-29 | 深圳市冠融辰环保科技有限公司 | A kind of multiple-effect vacuum evaporator high temperature goes out the salt preventing clogging up device out of salt effect |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 530007 Factory Buildings 1 and 2, Guangxi University Science and Technology Park, No.1 Gaoxin Second Road, Nanning City, Guangxi Zhuang Autonomous Region Patentee after: Guangxi Chenkang Biotechnology Co.,Ltd. Country or region after: China Address before: 530007 Factory Buildings 1 and 2, Guangxi University Science and Technology Park, No.1 Gaoxin Second Road, Nanning City, Guangxi Zhuang Autonomous Region Patentee before: NANNING VENUSSON BIO-TECHNOLOGY Co.,Ltd. Country or region before: China |
|
| CP03 | Change of name, title or address |