CN215886437U - Condensate recovery equipment and circulating water cooling system - Google Patents

Condensate recovery equipment and circulating water cooling system Download PDF

Info

Publication number
CN215886437U
CN215886437U CN202122262737.9U CN202122262737U CN215886437U CN 215886437 U CN215886437 U CN 215886437U CN 202122262737 U CN202122262737 U CN 202122262737U CN 215886437 U CN215886437 U CN 215886437U
Authority
CN
China
Prior art keywords
water
liquid level
collecting tank
level switch
pipeline
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202122262737.9U
Other languages
Chinese (zh)
Inventor
侯长波
魏英豪
李杨
王俊光
马向辉
尹海宝
李志永
彭珍
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing Shougang Co Ltd
Original Assignee
Beijing Shougang Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Beijing Shougang Co Ltd filed Critical Beijing Shougang Co Ltd
Priority to CN202122262737.9U priority Critical patent/CN215886437U/en
Application granted granted Critical
Publication of CN215886437U publication Critical patent/CN215886437U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

The utility model discloses a condensate water recovery device and a circulating water cooling system, which are used for recovering and utilizing condensate water discharged in industrial production. The condensed water recovery device comprises an input pipeline, a water collecting tank and an output pipeline which are sequentially communicated, wherein the communication position of the input pipeline and the water collecting tank is higher than the communication position of the output pipeline and the water collecting tank. The condensed water is input into the water collecting tank through the input pipeline and is collected and stored in the water collecting tank, and after the condensed water in the water collecting tank exceeds a certain content, the condensed water is added into the circulating water through the output pipeline. The utility model can improve the quality of the circulating water in the circulating water cooling system, prolong the service time of the circulating water, reduce the equipment operation cost and the production cost, save water resources and have better popularization and use values.

Description

Condensate recovery equipment and circulating water cooling system
Technical Field
The application belongs to the technical field of condensate water recycling, and particularly relates to a condensate water recycling device and a circulating water cooling system.
Background
In modern industrial production, in order to ensure normal production, cooling water systems are required to cool various devices, cooling water is recycled in various cooling water systems, and the recycled cooling water is called circulating cooling water or circulating water. Typically, the circulating water is neutral and weakly alkaline. After the circulating water cools the equipment, the circulating water can absorb heat discharged by the equipment, a large amount of circulating water is evaporated, and evaporated water vapor is dissipated into the air. Because the circulating water is continuously lost through the mode of vapor and comdenstion water, the concentration of various mineral substances and ions in the circulating water is higher and higher, and quality of water is worse and worse, and the circulating water at this moment can become incrustation scale in the pipeline, block up the pipeline and even cause the corruption to relevant equipment.
In order to improve the quality of the circulating water, a method of replacing the circulating water or continuously adding new circulating water to the circulating water cooling system is generally adopted. However, the two methods use a large amount of water, waste water resources, and increase the operation cost and production cost of equipment. The mode of continuously adding new circulating water is adopted to improve the water quality, so that the service time of the added circulating water is shorter and shorter, the water quality is worse and faster, vicious circle is formed, and the equipment of a circulating water cooling system is damaged.
Disclosure of Invention
In order to solve the technical problems, the utility model provides a condensate water recovery device and a circulating water cooling system, which can collect steam and condensate water discharged by the device in the production process, and add the condensed steam and condensate water into the circulating water cooling system, thereby improving the quality of circulating water, prolonging the service life of the circulating water, reducing the operation cost and the production cost of the device, and saving water resources.
The technical scheme adopted for realizing the purpose of the utility model is that the condensed water recovery equipment comprises an input pipeline, a water collecting tank and an output pipeline which are sequentially communicated, wherein the communication position of the input pipeline and the water collecting tank is higher than the communication position of the output pipeline and the water collecting tank; the water collecting tank comprises a tank body and at least one water-vapor separation filter element, the water-vapor separation filter element is positioned in the tank body and is arranged on a top plate of the tank body, and the water-vapor separation filter element is provided with an opening for communicating with the outside; and a valve is arranged on the output pipeline.
Optionally, the condensed water recovery device further comprises a control device, an upper limit liquid level switch and a lower limit liquid level switch; the upper limit liquid level switch and the lower limit liquid level switch are both arranged in the box body, the upper limit liquid level switch is higher than the lower limit liquid level switch, and the upper limit liquid level switch is lower than the opening position; the upper limit liquid level switch, the lower limit liquid level switch and the valve are all electrically connected with the control device.
Optionally, the condensed water recovery device further comprises an alarm device, and the alarm device is electrically connected with the control device.
Optionally, the header tank still includes the level gauge, the level gauge is installed the side of box, the height of the biggest scale of level gauge with the height of upper limit liquid level switch position is the same, the height of the minimum scale of level gauge with the height of liquid lower limit liquid level switch position is the same.
Optionally, an output water pump is arranged on the output pipeline, the valve is located between the output water pump and the water collecting tank, and the output water pump is electrically connected with the control device.
Optionally, the output pipeline is provided with at least two valves, and each valve is respectively located at two sides of the output water pump.
Optionally, an input water pump is arranged on the input pipeline.
Optionally, an anti-corrosion layer is arranged on the inner surface of the box body.
Optionally, the communication position between the input pipeline and the box body is located on the top plate of the box body or on the upper portion of the side face of the box body, and the communication position between the output pipeline and the box body is located on the bottom plate of the box body or on the lower portion of the side face of the box body.
Based on the same inventive concept, the application also provides a circulating water cooling system, which comprises the condensate water recovery device, wherein the condensate water recovery device is communicated with the circulating water cooling system through the output pipeline.
According to the technical scheme, the condensed water recovery device comprises an input pipeline, a water collecting tank and an output pipeline which are sequentially communicated. The communication position of the input pipeline and the water collecting tank is higher than that of the output pipeline and the water collecting tank, and the output pipeline is also provided with a valve which controls whether condensed water can be output from the water collecting tank through the output pipeline. The water collecting tank comprises a tank body and at least one water-vapor separation filter element, all the water-vapor separation filter elements are arranged on a top plate of the tank body, an opening for communicating with the outside is required to be arranged on each water-vapor separation filter element, the water-vapor separation filter elements can filter out water vapor and moisture in gas, when the gas with water and vapor and the condensed water enter the interior of the box body through the input pipeline, the liquid level in the interior of the box body gradually rises along with the inflow of the condensed water, the gas in the interior of the box body flows out of the water collecting tank through the water-vapor separation filter element under the action of water pressure, the liquid drops and the vapor in the gas in the box body are filtered by the vapor separation filter element and are left in the box body of the water collecting tank, and the liquid drops and the vapor are converged and condensed into water drops to flow into the original condensed water, when the condensed water in the box body reaches a certain content, a valve on the output pipeline is opened, and all the condensed water is added into the circulating water through the output pipeline.
Compared with the prior art, the condensate water recovery device provided by the utility model has the advantages that the structure is simple, the use is convenient, and the discharged water vapor and condensate water are collected and arranged and are added into the circulating water cooling system. Compared with most industrial water, the condensate water has extremely low content of dissolved ions and minerals, so that the quality of the circulating water can be improved by adding the condensate water into the circulating water, the service life of the circulating water is prolonged, the equipment operation cost and the production cost are reduced, and water resources are saved.
Drawings
FIG. 1 is a schematic structural diagram of a condensate recovery apparatus according to an embodiment of the present invention.
Fig. 2 is a sectional view of a sump in the condensate recovery apparatus of fig. 1.
Description of reference numerals: 1-a water collecting tank, 11-a tank body, 12-a water-vapor separation filter element, 13-an upper limit liquid level switch, 14-a lower limit liquid level switch and 15-a liquid level meter; 2-an input pipeline; 3-output pipeline, 31-valve, 32-output water pump.
Detailed Description
In order to make the present application more clearly understood by those skilled in the art to which the present application pertains, the following detailed description of the present application is made with reference to the accompanying drawings by way of specific embodiments.
The embodiment of the utility model provides a condensate water recovery device, which is used for recovering various kinds of discharged condensate water in industrial production, and adding the condensate water into circulating water to improve the quality of the circulating water and prolong the service life of the circulating water. The respective constituent elements of the condensate recovery apparatus will be described in detail as follows:
example 1:
the condensate water recovery device provided by the embodiment of the utility model comprises a water collecting tank 1, an input pipeline 2 and an output pipeline 3, wherein the input pipeline 2 is communicated with the water collecting tank 1, and the communication position of the input pipeline 2 and the water collecting tank 1 is higher than the communication position of the output pipeline 3 and the water collecting tank 1. The water collecting tank 1 comprises a tank body 11 and at least one water-vapor separation filter element 12, wherein the water-vapor separation filter element 12 is positioned in the tank body and is arranged on a top plate of the tank body, and the water-vapor separation filter element 12 is provided with an opening communicated with the outside. The water-vapor separation filter element 12 is a device capable of filtering liquid drops and vapor in gas, after the gas passes through the water-vapor separation filter element 12, the air is dissipated to the outside of the water collecting tank 1 from the opening of the water-vapor separation filter element 12, the liquid drops and the vapor in the gas are adsorbed in the water absorbing layer of the water-vapor separation filter element 12, and the water drops and the vapor are dripped from the water-vapor separation filter element 12 after the water drops are converged and condensed. The water-vapor separation filter element 12 is of a cylindrical tubular structure, one end of the water-vapor separation filter element 12 is arranged in a closed manner, and the closed surface can be a water-tight flat plate or a filter layer which is the same as the side surface of the water-vapor separation filter element 12; the other end of the water-vapor separation filter element 12 is provided with an opening. The utility model has no special requirements on the water-vapor separation filter element 12, and the specific operation can be realized by adopting a mature product on the market.
When installing steam separation filter core 12 on box 11, should set up the through-hole on the roof of box 11, the one end that steam separation filter core 12 sealed the setting is placed in the inside of box 11 through the through-hole, and steam separation filter core 12 is provided with open one end and is connected with the through-hole and install on the roof of box 11. The specific connection mode of the opening and the through hole is various, and a clamping piece with the size larger than that of the through hole can be arranged on the edge of the opening; a flange can also be arranged outside the opening and fixed on the top plate through the flange to enable the opening to be connected with the through hole. In order to ensure that the position of the opening is higher than the position of the upper limit liquid level switch 13 in the box body, a protruding structure can be arranged on the top plate, the top surface of the protruding structure is the highest position of the box body 11, the through hole is arranged on the protruding structure, and the water-vapor separation filter element 12 is arranged through the through hole.
In some cases, it is often necessary to drain the tank 11, and therefore a drainage device is further provided on the bottom surface of the tank, and the drainage device can thoroughly drain the water in the tank. Because the condensed water, the vapor and the air exist in the box body 11 at the same time for a long time, the inner wall of the box body 11 is easy to generate the conditions of oxidation corrosion and the like, the box body 11 is damaged, the condensed water in the box body can be polluted by products of oxidation reaction, and in order to avoid the phenomenon, an anti-corrosion layer is arranged in the box body 11.
Referring to fig. 1 and 2, two water-vapor separation filter elements 12 are installed on the inner side of the top of a box body 11 of the water collection tank 1, and both the two water-vapor separation filter elements 12 are arranged in an open manner. In the present embodiment, the water collection tank 1 further includes an upper limit liquid level switch 13, a lower limit liquid level switch 14, and a liquid level meter 15. The upper limit liquid level switch 13 and the lower limit liquid level switch 14 are arranged on the inner side face of the box body 11, the position of the upper limit liquid level switch 13 is higher than that of the lower limit liquid level switch 14, and the position of the upper limit liquid level switch 13 is lower than the position of an opening of the water-vapor separation filter element 12. The liquid level meter 15 is arranged on the side wall of the box body 11, the height of the lowest position of the liquid level meter 15 is the same as the position height of the lower limit liquid level switch 14, and the height of the highest position of the liquid level meter 15 is the same as the position height of the upper limit liquid level switch 13. There are various types of the liquid level meter 15, and particularly in the present embodiment, the liquid level meter 15 is a transparent tube liquid level meter.
The water collecting tank 1 is also communicated with an input pipeline 2 and an output pipeline 3, and the communication position of the input pipeline 2 and the water collecting tank 1 is higher than the communication position of the output pipeline 3 and the water collecting tank 1.
The input pipeline 2 is communicated with a structure for discharging condensed water by industrial production equipment, and the condensed water and gas with moisture and vapor are input into the box body 11 of the water collecting tank 1 through the input pipeline 2. Since the input pipe 2 inputs liquid and gas simultaneously, the communication position of the input pipe 2 and the water collecting tank 1 should be at a position higher than the tank body for the safety and stability of the input process, so as to prevent the tank body 11 from being unstable due to the excessive liquid level oscillation caused by the gas input into the water from the input pipe 2 as much as possible. When the structure of the device for discharging the condensed water cannot provide enough pressure so that the condensed water cannot be input into the tank 11 through the input pipeline 2, an input water pump can be arranged on the input pipeline 2, and the specific position of the input water pump on the input pipeline 2 is set according to the specific installation condition of the utility model.
The outlet pipe 3 is provided with a valve 31. When the level of the condensed water collected in the tank 11 reaches a certain height, the valve 31 is opened, and the condensed water in the tank is added into the circulating water through the output pipeline 3. In actual use, the output end of the output pipeline 3 may be higher than the communication position between the output pipeline 3 and the box body 11, and the condensed water cannot flow out of the box body 11, so that an output water pump 32 may be installed on the output pipeline 3, and the output water pump 32 may pump the condensed water from the box body 11 into the output pipeline 3 and provide power for the condensed water to flow in the output pipeline 3. Between the valve 31 and the box body 11, a filtering mechanism can be arranged to filter the condensed water for one time and then add the condensed water into the circulating water, so that the condensed water is ensured not to contain impurities.
Referring to fig. 1, in the present embodiment, the communication position between the input pipeline 2 and the box 11 is located between two openings of two water vapor separation filter elements 12 on the top plate of the box 11; the output pipeline 3 is communicated with the lower part of the side surface of the box body 11, the communication position is close to the bottom surface of the box body 11, two valves 31 and an output water pump 32 are further arranged on the output pipeline 3, and the output water pump 32 is positioned between the valve 31a and the valve 31 b.
The condensate recovery device provided by the embodiment further comprises a control device, and the upper limit liquid level switch 13, the lower limit liquid level switch 14, the valve 31 and the output water pump 32 are all electrically connected with the control device.
Example 2:
the embodiment of the utility model provides a circulating water cooling system matched with a centralized air compressor station, and the circulating water cooling system is communicated with a condensate water recovery device in the embodiment 1. The specific mode is that a dryer exists in the centralized air compressor station, an input pipeline 2 of the condensate water recovery device is communicated with a condensate water discharge port of the dryer, and an output pipeline 3 of the condensate water recovery device is communicated with a pipeline or a circulating water tank in a circulating water cooling system.
When the condensate water recovery device provided by the embodiment is adopted to recycle the condensate water, the operation is as follows:
the operator connects the input pipe 2 with the condensed water discharge port of the dryer, and the condensed water enters the input pipe 2 along with the gas containing liquid droplets and water vapor, and is input into the water collecting tank 1 from the top of the tank body 11 through the input pipe 2 under the action of air pressure and water pressure. Since the liquid level in the tank 11 rises, the gas containing liquid droplets and water vapor flows upward inside the tank 11 under pressure after entering the water collection tank 1. When the gas that contains liquid drop and vapor passes through water vapor separation filter core 12, the air passes through water vapor separation filter core 12 and outside water catch tank 1 from the uncovered loss of water vapor separation filter core 12, liquid drop and vapor then adsorbed on water vapor separation filter core 12, after liquid drop and vapor that water vapor separation filter core 12 adsorbed assemble, condense into the water drop, the water drop drips from water vapor separation filter core 12 and gets into the condensate water in the box 11. When the level of the condensed water in the box body 11 is higher than the upper limit liquid level switch 13, the upper limit liquid level switch 13 transmits information to the control device, the control device opens the valve 31 and the output water pump 32, and the output water pump 32 pumps the condensed water out of the box body 11 through the output pipeline 3 and adds the condensed water into the circulating water through the output pipeline 3. When the liquid level in the tank 11 is lower than the lower limit liquid level switch 14, the lower limit liquid level switch 14 transmits information to the control device, the control device operates the output water pump 32 to be closed or gradually closed after a certain time, and the valve 31 is closed after the output water pump 32 is closed. The condensed water in the box body 11 continues to rise after the output is stopped, and the above operation is repeated until the dryer stops inputting the condensed water into the input pipeline 2.
Through the embodiment, the utility model has the following beneficial effects or advantages:
1) the condensate recovery equipment that this embodiment provided carries out recycle as the comdenstion water of waste water discharge in with industrial production, very big saving the water resource, reduced the cost and the manufacturing cost of equipment operation.
2) The comdenstion water recovery plant that this embodiment provided adds the comdenstion water into circulating water, and the comdenstion water is the water that forms after condensing by vapor, and consequently dissolved ion and mineral substance content in the comdenstion water are extremely low, add the comdenstion water into circulating water not only can supply the circulating water, can also reduce the concentration of ion and mineral substance in the circulating water, improve the quality of water of circulating water, the live time of extension circulating water, the equipment that protection circulating water cooling system used.
While the preferred embodiments of the present application have been described, additional variations and modifications in those embodiments may occur to those skilled in the art once they learn of the basic inventive concepts. Therefore, it is intended that the appended claims be interpreted as including preferred embodiments and all alterations and modifications as fall within the scope of the application.
It will be apparent to those skilled in the art that various changes and modifications may be made in the present application without departing from the spirit and scope of the application. Thus, if such modifications and variations of the present application fall within the scope of the claims of the present application and their equivalents, the present application is intended to include such modifications and variations as well.

Claims (10)

1. A condensate recovery apparatus characterized in that: the device comprises an input pipeline, a water collecting tank and an output pipeline which are sequentially communicated, wherein the communication position of the input pipeline and the water collecting tank is higher than the communication position of the output pipeline and the water collecting tank; the water collecting tank comprises a tank body and at least one water-vapor separation filter element, the water-vapor separation filter element is positioned in the tank body and is arranged on a top plate of the tank body, and the water-vapor separation filter element is provided with an opening for communicating with the outside; and a valve is arranged on the output pipeline.
2. The condensate recovery apparatus of claim 1, wherein: the condensed water recovery device also comprises a control device, an upper limit liquid level switch and a lower limit liquid level switch; the upper limit liquid level switch and the lower limit liquid level switch are both arranged in the box body, the upper limit liquid level switch is higher than the lower limit liquid level switch, and the upper limit liquid level switch is lower than the opening position; the upper limit liquid level switch, the lower limit liquid level switch and the valve are all electrically connected with the control device.
3. The condensate recovery apparatus of claim 2, wherein: the condensed water recovery device further comprises an alarm device, and the alarm device is electrically connected with the control device.
4. The condensate recovery apparatus of claim 2, wherein: the water collecting tank further comprises a liquid level meter, the liquid level meter is installed on the side face of the tank body, the height of the maximum scale of the liquid level meter is the same as that of the upper limit liquid level switch position, and the height of the minimum scale of the liquid level meter is the same as that of the lower limit liquid level switch position.
5. The condensate recovery apparatus of claim 2, wherein: the output pipeline is provided with an output water pump, the valve is positioned between the output water pump and the water collecting tank, and the output water pump is electrically connected with the control device.
6. The condensate recovery apparatus of claim 5, wherein: the output pipeline is provided with at least two valves, and the valves are respectively positioned on two sides of the output water pump.
7. The condensate recovery apparatus according to any one of claims 1 to 6, wherein: and an input water pump is arranged on the input pipeline.
8. The condensate recovery apparatus according to any one of claims 1 to 6, wherein: and an anti-corrosion layer is arranged on the inner surface of the box body.
9. The condensate recovery apparatus according to any one of claims 1 to 6, wherein: the communication position of the input pipeline and the box body is positioned on the top plate of the box body or the upper part of the side surface of the box body, and the communication position of the output pipeline and the box body is positioned on the bottom plate of the box body or the lower part of the side surface of the box body.
10. A circulating water cooling system is characterized in that: a condensate recovery apparatus comprising the condensate recovery apparatus of any one of claims 1 to 9, the condensate recovery apparatus being in communication with the circulating water cooling system through the output conduit.
CN202122262737.9U 2021-09-17 2021-09-17 Condensate recovery equipment and circulating water cooling system Active CN215886437U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202122262737.9U CN215886437U (en) 2021-09-17 2021-09-17 Condensate recovery equipment and circulating water cooling system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202122262737.9U CN215886437U (en) 2021-09-17 2021-09-17 Condensate recovery equipment and circulating water cooling system

Publications (1)

Publication Number Publication Date
CN215886437U true CN215886437U (en) 2022-02-22

Family

ID=80349082

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202122262737.9U Active CN215886437U (en) 2021-09-17 2021-09-17 Condensate recovery equipment and circulating water cooling system

Country Status (1)

Country Link
CN (1) CN215886437U (en)

Similar Documents

Publication Publication Date Title
CN103785191B (en) The method that vinyl chloride high-boiling components rectifier unit and the rectifying of vinyl chloride high-boiling components are separated
CN215886437U (en) Condensate recovery equipment and circulating water cooling system
CN110926231A (en) High-efficient air cooling system
CN208204527U (en) A kind of steam trap connection of recyclable steam water
CN201199025Y (en) Automatic recovering device of condensed water
CN215637935U (en) Condensate water cooling and recovering system
CN211514001U (en) Improved chemical engineering tail gas absorption tower
CN208785947U (en) A kind of oil liquid vacuum intelligent filtering water scavenging system
CN209386269U (en) A kind of secondary steam high pressure regenerating unit
CN209052501U (en) Vacuum pump circulating water cooling system
CN207317561U (en) One kind is used for the simple way of escape vacuum extractor of unclean steam-electric power
CN220737002U (en) CO dewatering and separating system
CN213976977U (en) Waste sulfuric acid recovery device
CN220062644U (en) Nickel electrolysis condensate water recovery device
CN212769988U (en) Circulating separation type dewatering system for high-concentration oily wastewater
CN217889946U (en) Storage battery terminal welding device
CN219454717U (en) Vacuum exhaust condensation water-saving system of green mud filter
CN219743997U (en) Dewatering system for chemical production
CN219231503U (en) Automatic liquid-liquid separation equipment
CN216668355U (en) Air cooling island condensate treatment system
CN210905000U (en) Evaporator pollution discharge device
CN217163270U (en) A processing apparatus that is arranged in N-methylaniline production process vacuum pump peculiar smell
CN211585275U (en) Methanol steam emptying and recycling mechanism of pre-rectifying tower of methanol plant
CN219355290U (en) System for recovering flash evaporation condensate water during filament making
CN215979793U (en) Zero-gas-consumption drain valve

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant