CN112245954B - Liquid purifying equipment - Google Patents
Liquid purifying equipment Download PDFInfo
- Publication number
- CN112245954B CN112245954B CN202011273606.4A CN202011273606A CN112245954B CN 112245954 B CN112245954 B CN 112245954B CN 202011273606 A CN202011273606 A CN 202011273606A CN 112245954 B CN112245954 B CN 112245954B
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- liquid
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- pipeline
- air
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- 239000007788 liquid Substances 0.000 title claims abstract description 98
- 238000011084 recovery Methods 0.000 claims description 25
- 238000000746 purification Methods 0.000 claims description 9
- 238000003466 welding Methods 0.000 claims description 2
- 230000006978 adaptation Effects 0.000 claims 2
- 238000005516 engineering process Methods 0.000 description 7
- 238000009835 boiling Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000011031 large-scale manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000000652 homosexual effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/007—Energy recuperation; Heat pumps
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention provides liquid purifying equipment, which comprises a heat energy circulating system and a wind energy circulating system, and a liquid conveying system.
Description
Technical Field
The present invention relates to a liquid purification apparatus.
Background
At present, in the industries of medicine, chemical industry, light industry, beverage and the like, liquid purification generally adopts an adsorption medium to be placed in the liquid for adsorption purification, and then filtration and separation are carried out, and particularly, the solid-liquid mixture of the bottom foot is difficult to treat; the traditional technology of heating distillation extraction is also used, and the traditional technology is laggard and has low efficiency; patent number: the 2011104111654 patent name wine liquid impurity removing system and the impurity removing method have certain defects in impurity removing and separating at normal temperature; patent number: the system and the method for purifying the 2016103678241 patent name white spirit have certain limitations in realizing large-scale production under the condition of sunshine heating in a glass room; patent number: the 2013102801832 patent name is that the method for improving the white spirit grade is characterized in that the liquid is cooled and recovered step by step after the temperature is raised, the liquid is cooled and recovered at a low temperature after the temperature is raised, the liquid cold energy cannot be recovered seriously, so that the energy waste is caused, the equipment investment is large, the operation cost is high, and a certain gap exists in realizing the large-scale production; the large-scale production of the traditional technology is difficult to meet, the market is difficult to popularize, and the liquid purification technology is to be improved.
Disclosure of Invention
In order to solve the problems, the invention aims to provide the liquid purifying equipment which is simple to operate and easy to use, is scientific and reasonable, is simple, practical and efficient, realizes quick separation and continuous purification, and is more suitable for mass production.
The liquid purifying equipment comprises a heat energy circulating system and a wind energy circulating system, and a liquid conveying system;
The thermal energy circulation system: the outlet of the heat source tank 4 is connected with the inlet of the heat energy circulating pump 3 through a pipeline, the heat inlet of the heat exchanger 2 is connected with the outlet of the heat energy circulating pump 3 through a pipeline, the heat outlet of the heat exchanger 2 is connected with the inlet of the heat source tank 4 through a pipeline, wherein the heat energy of the heat source tank 4 is adaptively designed according to actual requirements, and the liquid for transferring the heat energy is adaptively designed according to working condition requirements;
the wind energy circulation system comprises: the outlet of the fan 8 is connected with the air inlet of the gas-liquid tank 9 through the air inlet pipe 5, the air inlet of the recovery device 7 is connected with the air outlet of the gas-liquid tank 9 through the air outlet pipe 6, the inlet of the fan 8 is connected with the air outlet of the recovery device 7 through a pipeline, and the potential positions of the air inlet and the air outlet of the inner cavity of the gas-liquid tank 9 are higher than the liquid level A of the gas-liquid tank 9;
the liquid delivery system: the cold inlet of the recovery heat exchanger 11 is connected with the outlet of the liquid inlet pump 1 through a pipeline, the cold inlet of the heat exchanger 2 is connected with the cold outlet of the recovery heat exchanger 11 through a pipeline, the liquid inlet of the gas liquid tank 9 is connected with the cold outlet of the heat exchanger 2 through a pipeline, the inlet of the delivery pump 10 is connected with the liquid outlet of the gas liquid tank 9 through a pipeline, the outlet of the delivery pump 10 is connected with the hot inlet of the recovery heat exchanger 11 through a pipeline, the inlet of the liquid inlet pump 1 is connected with a liquid inlet pipe, the hot outlet of the recovery heat exchanger 11 is connected with a liquid outlet pipe, the liquid inlet pipe is connected with the liquid outlet pipe through a valve 12, and the liquid outlet position of the gas liquid tank 9 is lower than the liquid level A of the gas liquid tank 9.
Drawings
Fig. 1 is a schematic diagram of the present invention, in which a liquid inlet pump 1, a heat exchanger 2, a heat energy circulation pump 3, a heat source tank 4, an air inlet pipe 5, an air outlet pipe 6, a recovery device 7, a fan 8, a gas-liquid tank 9, a transfer pump 10, a recovery heat exchanger 11, a valve 12, and a liquid level a.
Detailed Description
The present invention will now be described in further detail with reference to the accompanying drawings and the foregoing summary. The invention aims to provide liquid purifying equipment which is scientific, reasonable, simple, practical and efficient, realizes rapid separation and continuous purification and is more suitable for mass production.
In an embodiment, referring to fig. 1, the liquid purifying apparatus includes a thermal energy circulation system and a wind energy circulation system, and a liquid delivery system;
The thermal energy circulation system: the outlet of the heat source tank 4 is connected with the inlet of the heat energy circulating pump 3 through a pipeline, the heat inlet of the heat exchanger 2 is connected with the outlet of the heat energy circulating pump 3 through a pipeline, the heat outlet of the heat exchanger 2 is connected with the inlet of the heat source tank 4 through a pipeline, wherein the heat energy of the heat source tank 4 is adaptively designed according to actual requirements, and the liquid for transferring the heat energy is adaptively designed according to working condition requirements;
the wind energy circulation system comprises: the outlet of the fan 8 is connected with the air inlet of the gas-liquid tank 9 through the air inlet pipe 5, the air inlet of the recovery device 7 is connected with the air outlet of the gas-liquid tank 9 through the air outlet pipe 6, the inlet of the fan 8 is connected with the air outlet of the recovery device 7 through a pipeline, and the potential positions of the air inlet and the air outlet of the inner cavity of the gas-liquid tank 9 are higher than the liquid level A of the gas-liquid tank 9;
The liquid delivery system: the cold inlet of the recovery heat exchanger 11 is connected with the outlet of the liquid inlet pump 1 through a pipeline, the cold inlet of the heat exchanger 2 is connected with the cold outlet of the recovery heat exchanger 11 through a pipeline, the liquid inlet of the gas liquid tank 9 is connected with the cold outlet of the heat exchanger 2 through a pipeline, the inlet of the delivery pump 10 is connected with the liquid outlet of the gas liquid tank 9 through a pipeline, the outlet of the delivery pump 10 is connected with the hot inlet of the recovery heat exchanger 11 through a pipeline, the inlet of the liquid inlet pump 1 is connected with a liquid inlet pipe, the hot outlet of the recovery heat exchanger 11 is connected with a liquid outlet pipe, the liquid inlet pipe is connected with the liquid outlet pipe through a valve 12, and the liquid outlet position of the gas liquid tank 9 is lower than the liquid level A of the gas liquid tank 9;
the design scheme of the recovery device 7 is as follows: 1. when the low boiling point substances in the vapor state need to be purified and intercepted, the gas filtering and intercepting function is designed; 2. when the low-boiling point substance in the vapor state needs to be reduced to the liquid state, the liquid recovery function is designed to be realized by cooling and liquefying; 3. when the low-boiling point substances in the vapor state need to be reduced to the liquid state and the separated flowing air also needs to be purified and intercepted, the device is designed to realize the functions of cooling, liquefying, recovering liquid and filtering and intercepting gas; these functions are not described in detail as to general technical functions that will be relatively known to those skilled in the art.
The primary liquid purification equipment is adapted to design matching elements such as valves according to actual working condition requirements; the connection is not limited to grafting flanges, quick assembly, welding and the like, and is designed according to working conditions; the technology obtained by adding partial elements or reducing partial elements in the technology is slightly superior or inferior to the prior art, and belongs to the homosexual technology.
According to the working condition requirement, a semi-automatic, full-automatic and intelligent operation process can be designed.
Specifically, the operation is performed, the equipment condition is checked before the operation equipment is operated, all working procedures before the equipment is started are completed, purified liquid enters the recovery heat exchanger 11 through the liquid inlet pipe, then enters the heat exchanger 2 to heat up to the temperature of the material with low volatile boiling point, then enters the gas-liquid tank 9 to volatilize the material with low boiling point, the wind energy circulation system is circulated through the recovery device 7 to intercept the material with low volatile boiling point, and after the liquid is purified, the liquid is sent into the recovery heat exchanger 11 through the delivery pump 10 to recover heat energy, and then enters the liquid outlet pipe to realize continuous operation.
The device is scientific and reasonable, simple, practical and efficient, reduces the production cost, realizes quick separation and continuous purification, and is more suitable for mass production.
Claims (1)
1. A liquid purification apparatus comprising a thermal energy circulation system and a wind energy circulation system, a liquid delivery system, wherein the thermal energy circulation system: the outlet of the heat source tank (4) is connected with the inlet of the heat energy circulating pump (3) through a pipeline, the heat inlet of the heat exchanger (2) is connected with the outlet of the heat energy circulating pump (3) through a pipeline, and the heat outlet of the heat exchanger (2) is connected with the inlet of the heat source tank (4) through a pipeline, wherein the heat energy of the heat source tank (4) is generated according to the actual demand adaptation design, and the heat energy transferring liquid is according to the working condition demand adaptation design; the wind energy circulation system comprises: an outlet of the fan (8) is connected with an air inlet of the air liquid tank (9) through an air inlet pipe (5), an air inlet of the recovery device (7) is connected with an air outlet of the air liquid tank (9) through an air outlet pipe (6), an inlet of the fan (8) is connected with an air outlet of the recovery device (7) through a pipeline, and an air inlet and an air outlet of an inner cavity of the air liquid tank (9) are higher than the liquid level of the air liquid tank (9); the liquid delivery system: the cold inlet of the recovery heat exchanger (11) is connected with the outlet of the liquid inlet pump (1) through a pipeline, the cold inlet of the heat exchanger (2) is connected with the cold outlet of the recovery heat exchanger (11) through a pipeline, the liquid inlet of the gas liquid tank (9) is connected with the cold outlet of the heat exchanger (2) through a pipeline, the inlet of the delivery pump (10) is connected with the liquid outlet of the gas liquid tank (9) through a pipeline, the outlet of the delivery pump (10) is connected with the hot inlet of the recovery heat exchanger (11) through a pipeline, the inlet of the liquid inlet pump (1) is connected with a liquid inlet pipe, the hot outlet of the recovery heat exchanger (11) is connected with a liquid outlet pipe through a flange or a welding, the liquid inlet pipe is connected with the liquid outlet pipe through a valve (12), and the liquid outlet potential of the gas liquid tank (9) is lower than the liquid level of the gas liquid tank (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011273606.4A CN112245954B (en) | 2020-11-14 | 2020-11-14 | Liquid purifying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011273606.4A CN112245954B (en) | 2020-11-14 | 2020-11-14 | Liquid purifying equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN112245954A CN112245954A (en) | 2021-01-22 |
| CN112245954B true CN112245954B (en) | 2024-05-10 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011273606.4A Active CN112245954B (en) | 2020-11-14 | 2020-11-14 | Liquid purifying equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112245954B (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106986486A (en) * | 2017-05-10 | 2017-07-28 | 南京工业大学 | High organic effluent treatment plant that contains salt |
| CN108483542A (en) * | 2018-05-28 | 2018-09-04 | 昆山尚道源环境技术有限公司 | The evaporation of air circulation energy regenerating waste water divides salt system and wastewater treatment method |
| CN213760536U (en) * | 2020-11-14 | 2021-07-23 | 高云芝 | Liquid purifying equipment |
-
2020
- 2020-11-14 CN CN202011273606.4A patent/CN112245954B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106986486A (en) * | 2017-05-10 | 2017-07-28 | 南京工业大学 | High organic effluent treatment plant that contains salt |
| CN108483542A (en) * | 2018-05-28 | 2018-09-04 | 昆山尚道源环境技术有限公司 | The evaporation of air circulation energy regenerating waste water divides salt system and wastewater treatment method |
| CN213760536U (en) * | 2020-11-14 | 2021-07-23 | 高云芝 | Liquid purifying equipment |
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| Publication number | Publication date |
|---|---|
| CN112245954A (en) | 2021-01-22 |
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