CN214634079U - Two-stage heating purification equipment - Google Patents
Two-stage heating purification equipment Download PDFInfo
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- CN214634079U CN214634079U CN202022628428.4U CN202022628428U CN214634079U CN 214634079 U CN214634079 U CN 214634079U CN 202022628428 U CN202022628428 U CN 202022628428U CN 214634079 U CN214634079 U CN 214634079U
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Abstract
The utility model provides a second grade intensification clarification plant, include: first heat energy circulation system, first wind energy circulation system, second heat energy circulation system, second wind energy circulation system, liquid conveying system, this equipment scientific and reasonable, simple and practical high-efficient has realized quick fractionation and continuous purification, more is fit for mass production.
Description
Technical Field
The utility model relates to a second grade intensification clarification plant.
Background
At present, in the liquid purification of the industries such as medicine, chemical industry, light industry, beverage and the like, an adsorption medium is generally placed in liquid for adsorption and purification, and then filtration and separation are carried out, particularly, a solid-liquid mixture of the bottom foot is difficult to treat; the traditional technology is used for heating, distilling and extracting, so that the traditional process is backward and low in efficiency; patent numbers: 2011104111654 patent name wine liquid impurity removal system and method has certain disadvantages for impurity removal and separation at normal temperature; patent numbers: 2016103678241 patent name is that the white spirit impurity removal and purification system and method has certain limitation for realizing large-scale production by raising temperature by sunlight in a glass room; patent numbers: 2013102801832 patent name A method for improving the grade of white spirit, the liquid is cooled and recovered step by step after heating, cooling is carried out after heating, heat energy can not be recovered, cooling is carried out at low temperature to recover the liquid, the cold energy of the liquid can not be recovered seriously to cause energy waste, the equipment investment is large, the operation cost is high, and certain difference is realized in large-scale production; the scale production of the traditional technology is difficult to meet, the market is difficult to popularize, and the liquid purification technology needs to be improved.
Disclosure of Invention
In order to solve the problem, the utility model aims at providing a second grade intensification clarification plant of easy operation, easy-to-use, this equipment scientific and reasonable, simple and practical high-efficient has realized quick stage separation and continuous purification, more is fit for mass production.
The two-stage heating purification device comprises: the system comprises a first heat energy circulating system, a first wind energy circulating system, a second heat energy circulating system, a second wind energy circulating system and a liquid conveying system;
the first thermal energy cycle system: an outlet of the first heat source tank is connected with an inlet of a first heat energy circulating pump through a pipeline, a heat inlet of a first heat exchanger is connected with an outlet of the first heat energy circulating pump through a pipeline, a heat outlet of the first heat exchanger is connected with the inlet of the first heat source tank through a pipeline, wherein the generation of the heat energy of the first heat source tank is designed in an adaptive mode according to actual requirements, and liquid for transferring the heat energy is designed in an adaptive mode according to working condition requirements;
the first wind energy circulation system: the outlet of a first fan is connected with the air inlet of a first gas liquid tank through a first air inlet pipe, the air inlet of a first recovery device is connected with the air outlet of the first gas liquid tank through a first air outlet pipe, the inlet of the first fan is connected with the air outlet of the first recovery device through a pipeline, and the air inlet and the air outlet of the inner cavity of the first gas liquid tank are higher than the first liquid level A of the first gas liquid tank;
the second thermal energy cycle system: an outlet of the second heat source tank is connected with an inlet of a second heat energy circulating pump through a pipeline, a heat inlet of a second heat exchanger is connected with an outlet of the second heat energy circulating pump through a pipeline, a heat outlet of the second heat exchanger is connected with an inlet of the second heat source tank through a pipeline, wherein the generation of the heat energy of the second heat source tank is designed in an adaptive mode according to actual requirements, and liquid for transferring the heat energy is designed in an adaptive mode according to working condition requirements;
the second wind energy circulation system: the outlet of a second fan is connected with the air inlet of a second gas-liquid tank through a second air inlet pipe, the air inlet of a second recovery device is connected with the air outlet of the second gas-liquid tank through a second air outlet pipe, the inlet of the second fan is connected with the air outlet of the second recovery device through a pipeline, and the air inlet and the air outlet of the inner cavity of the second gas-liquid tank are higher than the liquid level B of the second liquid of the second gas-liquid tank;
the liquid delivery system: a cold inlet of a third recovery heat exchanger is connected with an outlet of a liquid inlet pump through a pipeline, a cold inlet of the first heat exchanger is connected with a cold outlet of the third recovery heat exchanger through a pipeline, a liquid inlet of a first gas-liquid tank is connected with a cold outlet of the first heat exchanger through a pipeline, an inlet of a second conveying pump is connected with a liquid outlet of the first gas-liquid tank through a pipeline, an outlet of the second conveying pump is connected with a hot and cold inlet of the second recovery heat exchanger through a pipeline, a cold inlet of the second heat exchanger is connected with a hot and cold outlet of the second recovery heat exchanger through a pipeline, a liquid inlet of the second gas-liquid tank is connected with a cold outlet of the second heat exchanger through a pipeline, an inlet of a third conveying pump is connected with a liquid outlet of the second gas-liquid tank through a pipeline, and a hot inlet of the second recovery heat exchanger is connected with an outlet of the third conveying pump through a pipeline, the third heat inlet of the third recovery heat exchanger is connected with the heat outlet of the second recovery heat exchanger through a pipeline, the heat outlet of the third recovery heat exchanger is connected with a liquid outlet pipe, the inlet of the liquid inlet pump is connected with a liquid inlet pipe, the liquid inlet pipe is connected with the liquid outlet pipe through a valve, and the liquid outlet of the first gas-liquid tank is lower than the first liquid level A of the first gas-liquid tank; and the potential level of the liquid outlet of the second gas-liquid tank is lower than the second liquid level B of the second gas-liquid tank.
Drawings
Fig. 1 is the utility model discloses a schematic diagram, first feed liquor pump 1, first heat exchanger 2, first heat energy circulating pump 3, first heat source jar 4, first intake pipe 5, first outlet duct 6, first recovery unit 7, first fan 8, first gas tank 9, first liquid level A, second delivery pump 10, second heat exchanger 11, second heat energy circulating pump 12, second heat source jar 13, second intake pipe 14, second outlet duct 15, second recovery unit 16, second fan 17, second gas tank 18, third delivery pump 19, second recovery heat exchanger 20, third recovery heat exchanger 21, big circulating valve 22, second liquid level B.
Detailed Description
The present invention will now be described in further detail with reference to the attached drawings and the above summary of the invention. The utility model aims at providing a second grade intensification clarification plant, the utility model discloses equipment scientific and reasonable, simple and practical high-efficient has realized quickly separating and has purified in succession, has reduced manufacturing cost, more is fit for mass production.
In an embodiment, referring to fig. 1, the two-stage temperature-rising purification device performs temperature-rising purification in 2 stages according to different boiling points of purified substances, and comprises the following steps:
the multistage warming purification device comprises: the system comprises a first heat energy circulating system, a first wind energy circulating system, a second heat energy circulating system, a second wind energy circulating system and a liquid conveying system;
the first thermal energy cycle system: an outlet of a first heat source tank 4 is connected with an inlet of a first heat energy circulating pump 3 through a pipeline, a heat inlet of a first heat exchanger 2 is connected with an outlet of the first heat energy circulating pump 3 through a pipeline, a heat outlet of the first heat exchanger 2 is connected with an inlet of the first heat source tank 4 through a pipeline, wherein the heat energy of the first heat source tank 4 is adaptively designed according to actual requirements, and liquid for transferring heat energy is adaptively designed according to working condition requirements;
the first wind energy circulation system: an outlet of a first fan 8 is connected with an air inlet of a first gas liquid tank 9 through a first air inlet pipe 5, an air inlet of a first recovery device 7 is connected with an air outlet of the first gas liquid tank 9 through a first air outlet pipe 6, an inlet of the first fan 8 is connected with an air outlet of the first recovery device 7 through a pipeline, and the air inlet and the air outlet of an inner cavity of the first gas liquid tank 9 are higher than a first liquid level A of the first gas liquid tank 9;
the second thermal energy cycle system: an outlet of the second heat source tank 13 is connected with an inlet of a second heat energy circulating pump 12 through a pipeline, a heat inlet of the second heat exchanger 11 is connected with an outlet of the second heat energy circulating pump 12 through a pipeline, a heat outlet of the second heat exchanger 11 is connected with an inlet of the second heat source tank 13 through a pipeline, wherein the heat energy of the second heat source tank 13 is adaptively designed according to actual requirements, and liquid for transferring heat energy is adaptively designed according to working condition requirements;
the second wind energy circulation system: an outlet of a second fan 17 is connected with an air inlet of a second gas-liquid tank 18 through a second air inlet pipe 14, an air inlet of a second recovery device 16 is connected with an air outlet of the second gas-liquid tank 18 through a second air outlet pipe 15, an inlet of the second fan 17 is connected with an air outlet of the second recovery device 16 through a pipeline, and the air inlet and the air outlet of an inner cavity of the second gas-liquid tank 18 are higher than a second liquid level B of the second gas-liquid tank 18;
the liquid delivery system: a cold inlet of a third recovery heat exchanger 21 is connected with an outlet of a liquid inlet pump 1 through a pipeline, a cold inlet of the first heat exchanger 2 is connected with a cold outlet of the third recovery heat exchanger 21 through a pipeline, a liquid inlet of the first gas liquid tank 9 is connected with a cold outlet of the first heat exchanger 2 through a pipeline, an inlet of a second conveying pump 10 is connected with a liquid outlet of the first gas liquid tank 9 through a pipeline, an outlet of the second conveying pump 10 is connected with a cold inlet of a second recovery heat exchanger heat 20 through a pipeline, a cold inlet of the second heat exchanger 11 is connected with a cold outlet of the second recovery heat exchanger heat 20 through a pipeline, a liquid inlet of the second gas liquid tank 18 is connected with a cold outlet of the second heat exchanger 11 through a pipeline, an inlet of a third conveying pump 19 is connected with a liquid outlet of the second gas liquid tank 18 through a pipeline, and a hot inlet of the second recovery heat exchanger heat 20 is connected with an outlet of the third conveying pump 19 through a pipeline, the heat inlet of the third recovery heat exchanger 21 is connected with the heat outlet of the second recovery heat exchanger 20 through a pipeline, the heat outlet of the third recovery heat exchanger 21 is connected, the heat outlet of the recovery heat exchanger 21 is connected with a liquid outlet pipe, the inlet of the liquid inlet pump 1 is connected with a liquid inlet pipe, wherein the liquid inlet pipe and the liquid outlet pipe are connected through a valve 12, and the liquid outlet of the first gas-liquid tank 9 is lower than the first liquid level A of the first gas-liquid tank 9; the potential of the liquid outlet of the second gas-liquid tank 18 is lower than the second liquid level B of the second gas-liquid tank 18;
design of the first recovery device 7 and the second recovery device 16: 1. when the low-boiling-point substances in a vapor state need to be purified and intercepted, the gas filtering and intercepting function is designed; 2. when the material with low boiling point in the vapor state needs to be reduced into the liquid state, the function of cooling, liquefying and recovering the liquid is designed; 3. when the substances with low boiling points in the vapor state need to be reduced into the liquid state and the separated flowing air needs to be purified and intercepted, the device is designed to be multifunctional for cooling, liquefying and recovering liquid and filtering and intercepting gas; these several functions are not described in detail in general technical terms, which are well known to those skilled in the art.
The secondary heating purification equipment is adapted to design matched elements such as a valve and the like according to the requirements of actual working conditions; the connection is not limited to grafting flanges, quick assembly, welding and the like, and is designed according to working condition adaptation; 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 same-class technology.
According to the working condition requirement, a semi-automatic, full-automatic and intelligent operation process can be designed.
Specifically, the equipment condition is checked before the equipment is operated, all processes before the equipment is started are completed, then the purified liquid enters a third recovery heat exchanger 21 through the liquid inlet pipe, then enters the first heat exchanger 2 to be heated to reach the temperature of the substances with the first-stage low boiling point of volatilization, then enters the first gas liquid tank 9 to volatilize the substances with the first-stage low boiling point, the first wind energy circulating system circularly intercepts the substances with the first-stage low boiling point of volatilization through the first recovery device 7, the liquid is sent to the second recovery heat exchanger 20 through the second delivery pump 10 after being primarily purified, then enters the second heat exchanger 11 to be heated to reach the temperature of the substances with the second-stage low boiling point of volatilization, then enters the second gas liquid tank 18 to volatilize the substances with the second-stage low boiling point, and the second wind energy circulating system circularly intercepts the substances with the second-stage low boiling point of volatilization through the second recovery device 16, the liquid after the secondary purification is sent to the second recovery heat exchanger 20 through the third delivery pump 19 to recover heat energy, then enters the third recovery heat exchanger 21 to continue recovering heat energy, and then enters the liquid outlet pipe to realize continuous work.
The utility model discloses beneficial effect, equipment scientific and reasonable, simple and practical high-efficient has reduced manufacturing cost, has realized quickly separating and has purified in succession, more is fit for mass production.
Claims (6)
1. A two-stage heating purification device is characterized by comprising: the system comprises a first heat energy circulating system, a first wind energy circulating system, a second heat energy circulating system, a second wind energy circulating system and a liquid conveying system; the first thermal energy circulation system comprises a first heat exchanger (2), the first wind energy circulation system comprises a first gas liquid tank (9), the second thermal energy circulation system comprises a second heat exchanger (11), and the second wind energy circulation system comprises a second gas liquid tank (18); the liquid conveying system is connected with the first heat exchanger (2), the first gas-liquid tank (9), the second heat exchanger (11) and the second gas-liquid tank (18) in series through pipelines.
2. The two-stage temperature rising purification device according to claim 1, wherein the first thermal energy circulation system is: the outlet of the first heat source tank (4) is connected with the inlet of the first heat energy circulating pump (3) through a pipeline, the heat inlet of the first heat exchanger (2) is connected with the outlet of the first heat energy circulating pump (3) through a pipeline, the heat outlet of the first heat exchanger (2) is connected with the inlet of the first heat source tank (4) through a pipeline, and the heat energy of the first heat source tank (4) is generated according to the actual requirement adaptive design and the liquid for transferring the heat energy is designed according to the working condition requirement adaptive design.
3. The two-stage temperature rising purification device according to claim 2, wherein the first wind energy circulation system is: an outlet of a first fan (8) is connected with an air inlet of a first gas liquid tank (9) through a first air inlet pipe (5), an air inlet of a first recovery device (7) is connected with an air outlet of the first gas liquid tank (9) through a first air outlet pipe (6), an inlet of the first fan (8) is connected with an air outlet of the first recovery device (7) through a pipeline, and the air inlet and the air outlet of an inner cavity of the first gas liquid tank (9) are higher than a first liquid level (A) of the first gas liquid tank (9).
4. The two-stage temperature rising purification device according to claim 3, wherein the second thermal energy circulation system is characterized in that: the export of second heat source jar (13) passes through pipeline and second heat energy circulating pump (12) access connection, the hot import of second heat exchanger (11) pass through the pipeline with second heat energy circulating pump (12) exit connection, the hot export of second heat exchanger (11) pass through the pipeline with second heat source jar (13) access connection, wherein the production of second heat source jar (13) heat energy is according to actual demand adaptation design, the liquid of transfer heat energy is according to operating mode demand adaptation design.
5. The two-stage temperature rising purification device according to claim 4, wherein the second wind energy circulation system is: an outlet of the second fan (17) is connected with an air inlet of the second gas liquid tank (18) through a second air inlet pipe (14), an air inlet of the second recovery device (16) is connected with an air outlet of the second gas liquid tank (18) through a second air outlet pipe (15), an inlet of the second fan (17) is connected with an air outlet of the second recovery device (16) through a pipeline, and the air inlet and the air outlet of an inner cavity of the second gas liquid tank (18) are higher than a second liquid level (B) of the second gas liquid tank (18).
6. The two-stage temperature rising purification apparatus according to claim 5, wherein the liquid delivery system: a cold inlet of a third recovery heat exchanger (21) is connected with an outlet of a liquid inlet pump (1) through a pipeline, a cold inlet of the first heat exchanger (2) is connected with a cold outlet of the third recovery heat exchanger (21) through a pipeline, a liquid inlet of a first gas-liquid tank (9) is connected with the cold outlet of the first heat exchanger (2) through a pipeline, an inlet of a second conveying pump (10) is connected with a liquid outlet of the first gas-liquid tank (9) through a pipeline, an outlet of the second conveying pump (10) is connected with a cold inlet of a second recovery heat exchanger (20) through a pipeline, a cold inlet of the second heat exchanger (11) is connected with a cold outlet of the second recovery heat exchanger (20) through a pipeline, a liquid inlet of the second gas-liquid tank (18) is connected with a cold outlet of the second heat exchanger (11) through a pipeline, and an inlet of a third conveying pump (19) is connected with a liquid outlet of the second gas-liquid tank (18) through a pipeline, the heat inlet of the second recovery heat exchanger (20) is connected with the outlet of the third delivery pump (19) through a pipeline, the heat inlet of the third recovery heat exchanger (21) is connected with the heat outlet of the second recovery heat exchanger (20) through a pipeline, the heat outlet of the third recovery heat exchanger (21) is connected with a liquid outlet pipe, the inlet of the liquid inlet pump (1) is connected with a liquid inlet pipe, the liquid inlet pipe and the liquid outlet pipe are connected through a valve, and the liquid outlet of the first gas-liquid tank (9) is lower than the first liquid level (A) of the first gas-liquid tank (9); the potential of the liquid outlet of the second gas-liquid tank (18) is lower than the second liquid level (B) of the second gas-liquid tank (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022628428.4U CN214634079U (en) | 2020-11-14 | 2020-11-14 | Two-stage heating purification equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022628428.4U CN214634079U (en) | 2020-11-14 | 2020-11-14 | Two-stage heating purification equipment |
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| CN214634079U true CN214634079U (en) | 2021-11-09 |
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| CN202022628428.4U Withdrawn - After Issue CN214634079U (en) | 2020-11-14 | 2020-11-14 | Two-stage heating purification equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112245953A (en) * | 2020-11-14 | 2021-01-22 | 高云芝 | Two-stage heating purification equipment |
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2020
- 2020-11-14 CN CN202022628428.4U patent/CN214634079U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112245953A (en) * | 2020-11-14 | 2021-01-22 | 高云芝 | Two-stage heating purification equipment |
| CN112245953B (en) * | 2020-11-14 | 2024-05-10 | 高云芝 | Two-stage heating purifying equipment |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20211109 Effective date of abandoning: 20230808 |