CN213760536U - Liquid purifying equipment - Google Patents
Liquid purifying equipment Download PDFInfo
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- CN213760536U CN213760536U CN202022628429.9U CN202022628429U CN213760536U CN 213760536 U CN213760536 U CN 213760536U CN 202022628429 U CN202022628429 U CN 202022628429U CN 213760536 U CN213760536 U CN 213760536U
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Abstract
The utility model provides a liquid purifying equipment, including heat energy circulating system and wind energy circulating system, liquid conveying system, this equipment scientific and reasonable, simple and practical high-efficient has realized quickly separating and has purified in succession, more is fit for mass production.
Description
Technical Field
The present invention relates to a liquid purification apparatus.
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 liquid clarification plant easy operation, easy-to-use, this equipment scientific and reasonable, simple and practical high-efficient has realized quick separation and continuous purification, more is fit for mass production.
The liquid purification equipment comprises a heat energy circulating system, a wind energy circulating system and a liquid conveying system;
the heat energy circulating system comprises: an outlet of the heat source tank is connected with an inlet of a heat energy circulating pump through a pipeline, a heat inlet of a heat exchanger is connected with an outlet of the heat energy circulating pump through a pipeline, a heat outlet of the heat exchanger is connected with the inlet of the heat source tank through a pipeline, wherein the heat energy of the heat source tank is adaptively designed according to actual requirements, and liquid for transferring heat energy is adaptively designed according to working condition requirements;
the wind energy circulating system comprises: the outlet of the fan is connected with the air inlet of the gas-liquid tank through an air inlet pipe, the air inlet of the recovery device is connected with the air outlet of the gas-liquid tank through an air outlet pipe, the inlet of the fan is connected with the air outlet of the recovery device through a pipeline, and the air inlet and the air outlet of the inner cavity of the gas-liquid tank are higher than the liquid level A of the gas-liquid tank;
the liquid delivery system: retrieve the cold import of heat exchanger and pass through pipeline and feed liquor pump exit linkage, heat exchanger's cold import pass through the pipeline with retrieve the cold exit linkage of heat exchanger, the gas liquid jar inlet pass through the pipeline with heat exchanger's cold exit linkage, the import of delivery pump pass through the pipeline with the gas-liquid jar liquid outlet is connected, the export of delivery pump passes through the pipeline and connects retrieve the heat exchanger heat import, feed liquor pump access connection feed liquor pipe, retrieve heat exchanger heat exit linkage drain pipe, wherein the feed liquor pipe with the drain pipe passes through the valve and connects, the potential position of gas liquid jar liquid outlet is less than the liquid level A of gas liquid jar.
Drawings
Fig. 1 is a schematic diagram of the present invention, which comprises a liquid inlet pump 1, a heat exchanger 2, a heat energy circulating pump 3, a heat source tank 4, a gas inlet pipe 5, a gas outlet pipe 6, a recovery device 7, a fan 8, a gas-liquid tank 9, a delivery 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 attached drawings and the above summary of the invention. The invention aims to provide liquid purification equipment which is scientific, reasonable, simple, practical and efficient, realizes quick separation and continuous purification and is more suitable for mass production.
In an embodiment, referring to fig. 1, the liquid purification apparatus includes a thermal energy circulation system, a wind energy circulation system, and a liquid delivery system;
the heat energy circulating system comprises: an outlet of a heat source tank 4 is connected with an inlet of a heat energy circulating pump 3 through a pipeline, a heat inlet of a heat exchanger 2 is connected with an outlet of the heat energy circulating pump 3 through a pipeline, a heat outlet of the heat exchanger 2 is connected with an 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 liquid for transferring heat energy is adaptively designed according to working condition requirements;
the wind energy circulating system comprises: an outlet of a fan 8 is connected with an air inlet of a gas-liquid tank 9 through an air inlet pipe 5, an air inlet of a recovery device 7 is connected with an air outlet of the gas-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 the air inlet and the air outlet of an 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: a cold inlet of a recovery heat exchanger 11 is connected with an outlet of a liquid inlet pump 1 through a pipeline, a cold inlet of the heat exchanger 2 is connected with a cold outlet of the recovery heat exchanger 11 through a pipeline, a liquid inlet of a gas liquid tank 9 is connected with a cold outlet of the heat exchanger 2 through a pipeline, an inlet of a conveying pump 10 is connected with a liquid outlet of the gas liquid tank 9 through a pipeline, an outlet of the conveying pump 10 is connected with a hot inlet of the recovery heat exchanger 11 through a pipeline, an inlet of the liquid inlet pump 1 is connected with a liquid inlet pipe, a hot outlet of the recovery heat exchanger 11 is connected with a liquid outlet pipe, wherein the liquid inlet pipe and the liquid outlet pipe are connected through a valve 12, and the liquid outlet of the gas liquid tank 9 is lower than the liquid level A of the gas liquid tank 9;
design of the recovery device 7: 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 primary liquid 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 operation equipment, all processes before starting the equipment are completed, purified liquid enters the recovery heat exchanger 11 through the liquid inlet pipe, then enters the heat exchanger 2 to be heated to reach the temperature of substances with low volatilization boiling points, and then enters the gas liquid tank 9 to volatilize the substances with low boiling points, the wind energy circulating system circulates through the recovery device 7 to intercept the substances with low volatilization boiling points, the liquid is purified and then sent to the recovery heat exchanger 11 through the delivery pump 10 to recover heat energy, and then enters the liquid outlet pipe, and continuous work is realized.
The utility model discloses equipment scientific and reasonable, simple and practical high-efficient, use cost is cheap, has realized quick separation and continuous purification, more is fit for mass production.
Claims (1)
1. A liquid purification apparatus, includes heat energy circulation system and wind energy circulation system, liquid delivery system, its characterized in that, heat energy circulation system: an outlet of the heat source tank (4) is connected with an inlet of a heat energy circulating pump (3) through a pipeline, a heat inlet of the heat exchanger (2) is connected with an outlet of the heat energy circulating pump (3) through a pipeline, a heat outlet of the heat exchanger (2) is connected with an 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 liquid for transferring heat energy is adaptively designed according to working condition requirements;
the wind energy circulating system comprises: an outlet of a fan (8) is connected with an air inlet of a gas-liquid tank (9) through an air inlet pipe (5), an air inlet of a recovery device (7) is connected with an air outlet of the gas-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 the air inlet and the air outlet of an 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: retrieve heat exchanger (11) cold import and pass through pipeline and feed liquor pump (1) exit linkage, the cold import of heat exchanger (2) pass through the pipeline with retrieve heat exchanger (11) cold exit linkage, gas liquid jar (9) inlet pass through the pipeline with the cold exit linkage of heat exchanger (2), the import of delivery pump (10) pass through the pipeline with gas liquid jar (9) liquid outlet is connected, the export of delivery pump (10) passes through the pipe connection retrieve heat exchanger (11) hot import, feed liquor pump (1) access connection feed liquor pipe, retrieve heat exchanger (11) hot exit linkage drain pipe, wherein the feed liquor pipe with the drain pipe passes through valve (12) and connects, gas liquid jar (9) liquid outlet potential position is less than liquid level (A) of gas liquid jar (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022628429.9U CN213760536U (en) | 2020-11-14 | 2020-11-14 | Liquid purifying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022628429.9U CN213760536U (en) | 2020-11-14 | 2020-11-14 | Liquid purifying equipment |
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| CN213760536U true CN213760536U (en) | 2021-07-23 |
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| CN202022628429.9U Active CN213760536U (en) | 2020-11-14 | 2020-11-14 | Liquid purifying equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112245954B (en) * | 2020-11-14 | 2024-05-10 | 高云芝 | Liquid purifying equipment |
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2020
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112245954B (en) * | 2020-11-14 | 2024-05-10 | 高云芝 | Liquid purifying equipment |
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