CN213220988U - Evaporator condensation water cooling system - Google Patents
Evaporator condensation water cooling system Download PDFInfo
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- CN213220988U CN213220988U CN202021962911.XU CN202021962911U CN213220988U CN 213220988 U CN213220988 U CN 213220988U CN 202021962911 U CN202021962911 U CN 202021962911U CN 213220988 U CN213220988 U CN 213220988U
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- cooling system
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Abstract
The utility model discloses an evaporimeter comdenstion water cooling system, including knockout tower, heat exchanger and cooling tower, the upper portion left side of knockout tower is connected with the inlet pipe, the inner chamber upper portion of knockout tower is equipped with the filter, the upper portion right side of knockout tower is in the upper portion left side of heat exchanger through first pipe connection, the lower part right side of knockout tower passes through the lower part left side of second pipe connection in heat exchanger, be equipped with exhaust fan on the second pipeline, the upper portion right side of heat exchanger passes through the third pipe connection in the left side upper portion of cooling tower, the bottom of cooling tower is passed through the fourth pipe connection in the bottom of heat exchanger, be equipped with the circulating pump on the fourth pipe, the lower part right side of heat exchanger is connected with the comdenstion water discharge pipe. The water molecules generated by evaporation of the utility model become secondary steam to be discharged, and then are condensed into condensed water to be discharged after reaching the standard; and the exhaust fan micropressure cooling mode is adopted, so that the energy consumption is saved, and the use cost of the pipeline is reduced.
Description
Technical Field
The utility model relates to an evaporimeter technical field specifically is an evaporimeter condensation water cooling system.
Background
The evaporator is required to be used for treating generated liquid in the chemical, food, pharmaceutical and sewage treatment industries, the condenser and the vacuum pump are commonly used for condensing condensate water of the existing evaporator, great pressure is generated on a pipeline, the pipeline with good quality is required to be used, the pipeline cost is increased, energy consumption is further increased due to the use of the vacuum pump, and therefore the evaporator condensate water cooling system is provided.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an evaporimeter condensation water cooling system to solve the problem that proposes among the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides an evaporimeter condensate water cooling system, includes knockout tower, heat exchanger and cooling tower, the upper portion left side of knockout tower is connected with the inlet pipe, the inner chamber upper portion of knockout tower is equipped with the filter, the upper portion right side of knockout tower is in the upper portion left side of heat exchanger through first pipe connection, the lower part right side of knockout tower passes through the second pipe connection in the lower part left side of heat exchanger, be equipped with exhaust fan on the second pipeline, the upper portion right side of heat exchanger passes through the third pipe connection in the left side upper portion of cooling tower, the bottom of cooling tower is passed through the fourth pipe connection in the bottom of heat exchanger, be equipped with the circulating pump on the fourth pipeline, the lower part right side of heat exchanger is connected with the comdens.
As a further optimization of the technical scheme, the separation tower, the heat exchanger and the cooling tower are sequentially arranged from left to right.
As a further optimization of the technical scheme, the inner cavity of the separation tower forms a secondary steam collecting cavity and an evaporation circulating liquid collecting cavity from top to bottom through a filter.
As a further optimization of the technical scheme, the feeding pipe extends into a nozzle fixed at the top of the secondary steam collecting cavity.
As a further optimization of the technical scheme, a discharge pipe communicated with the evaporation circulating liquid collecting cavity is arranged at the bottom of the separation tower.
Compared with the prior art, the beneficial effects of the utility model are that: the utility model discloses under the ordinary pressure condition, evaporating temperature can reach 40 degrees. And water molecules generated by evaporation are changed into secondary steam to be discharged, and then the secondary steam is condensed into condensed water to be discharged after reaching the standard. The organic matter, heavy metal and other harmful matter are stored in the concentrated liquid and exhausted automatically after reaching certain concentration. And the exhaust fan micropressure cooling mode is adopted, so that the energy consumption is saved, and the use cost of the pipeline is reduced.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
In the figure: 1 feeding pipe, 2 separating towers, 3 first pipelines, 4 discharging pipes, 5 exhaust fans, 6 heat exchangers, 7 circulating pumps, 8 condensed water discharging pipelines, 9 cooling towers, 10 fourth pipelines, 11 second pipelines, 12 filters and 13 third pipelines.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1, the present invention provides a technical solution: the utility model provides an evaporimeter condensate water cooling system, includes knockout tower 2, heat exchanger 6 and cooling tower 9, the upper portion left side of knockout tower 2 is connected with inlet pipe 1, the inner chamber upper portion of knockout tower 2 is equipped with filter 12, the upper portion right side of knockout tower 2 is connected in the upper portion left side of heat exchanger 6 through first pipeline 3, the lower part right side of knockout tower 2 is connected in the lower part left side of heat exchanger 6 through second pipeline 11, be equipped with exhaust fan 5 on the second pipeline 11, the upper portion right side of heat exchanger 6 is connected in the left side upper portion of cooling tower 9 through third pipeline 13, the bottom of cooling tower 9 is connected in the bottom of heat exchanger 6 through fourth pipeline 10, be equipped with circulating pump 7 on the fourth pipeline 10, the lower part right side of heat exchanger 6 is connected with comdenstion water discharge pipeline 8.
Specifically, the separation tower 2, the heat exchanger 6 and the cooling tower 9 are arranged from left to right in sequence.
Specifically, the inner cavity of the separation tower 2 forms a secondary steam collecting cavity and an evaporation circulating liquid collecting cavity from top to bottom through a filter 12.
Specifically, the feeding pipe 1 extends into a nozzle fixed at the top of the secondary steam collecting cavity.
Specifically, the bottom of the separation tower 2 is provided with a discharge pipe 4 communicated with the evaporation circulating liquid collecting cavity.
Specifically, when the device is used, heated materials enter the separation tower 2 through the feeding pipe 1, and after continuous heating circulation, concentrated solution separated from the separation tower 2 is discharged through the discharge pipe 4;
the secondary steam of the separation tower 2 is led out through the first pipeline 3, is pumped into the heat exchanger 6 for cooling under the work of the exhaust fan 5, then enters the separation tower 2 through the second pipeline 11, the aeration is added to the feed liquid, the condensate water generated after the heat exchange is discharged through the condensate water discharge pipeline 8, and the cooling water of the cooling tower 9 is continuously circulated through the heat exchanger 6 by the circulating pump 7.
The evaporator cooling system can be used in places without industrial steam, adopts an air energy heating source or other heat sources, indirectly heats, continuously evaporates and has no dirt, and is energy-saving, safe and convenient to clean. Therefore, the evaporator is suitable for materials with high viscosity, easy scaling and heat sensitivity, and is particularly suitable for evaporation of materials with special temperature requirements. Can be widely used in chemical, food, pharmaceutical and sewage treatment industries.
The evaporator condensed water cooling system can be used in places without industrial steam, adopts an air energy heating source or other heat sources, indirectly heats, continuously evaporates and has no dirt, and is energy-saving, safe and convenient to clean. Therefore, the evaporator is suitable for materials with high viscosity, easy scaling and heat sensitivity, and is particularly suitable for evaporation of materials with special temperature requirements. Can be widely used in chemical, food, pharmaceutical and sewage treatment industries.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (5)
1. An evaporator condensate water cooling system, comprising a separation tower (2), a heat exchanger (6) and a cooling tower (9), characterized in that: the left side edge of the upper part of the separation tower (2) is connected with a feeding pipe (1), the upper part of the inner cavity of the separation tower (2) is provided with a filter (12), the right side of the upper part of the separation tower (2) is connected with the left side of the upper part of the heat exchanger (6) through a first pipeline (3), the right side of the lower part of the separation tower (2) is connected with the left side of the lower part of the heat exchanger (6) through a second pipeline (11), an exhaust fan (5) is arranged on the second pipeline (11), the right side of the upper part of the heat exchanger (6) is connected with the upper part of the left side of the cooling tower (9) through a third pipeline (13), the bottom of the cooling tower (9) is connected with the bottom of the heat exchanger (6) through a fourth pipeline (10), and a circulating pump (7) is arranged on the fourth pipeline (10), and a condensed water discharge pipeline (8) is connected to the right side of the lower part of the heat exchanger (6).
2. An evaporator condensate cooling system according to claim 1, wherein: the separation tower (2), the heat exchanger (6) and the cooling tower (9) are sequentially arranged from left to right.
3. An evaporator condensate cooling system according to claim 1, wherein: the inner cavity of the separation tower (2) forms a secondary steam collecting cavity and an evaporation circulating liquid collecting cavity from top to bottom through a filter (12).
4. An evaporator condensate cooling system according to claim 3, wherein: the feeding pipe (1) extends into a nozzle fixed at the top of the secondary steam collecting cavity.
5. An evaporator condensate cooling system according to claim 3, wherein: and a discharge pipe (4) communicated with the evaporation circulating liquid collecting cavity is arranged at the bottom of the separation tower (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021962911.XU CN213220988U (en) | 2020-09-10 | 2020-09-10 | Evaporator condensation water cooling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021962911.XU CN213220988U (en) | 2020-09-10 | 2020-09-10 | Evaporator condensation water cooling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213220988U true CN213220988U (en) | 2021-05-18 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021962911.XU Active CN213220988U (en) | 2020-09-10 | 2020-09-10 | Evaporator condensation water cooling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213220988U (en) |
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2020
- 2020-09-10 CN CN202021962911.XU patent/CN213220988U/en active Active
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