CN108168336B - Condensation water residual heat recovery system - Google Patents
Condensation water residual heat recovery system Download PDFInfo
- Publication number
- CN108168336B CN108168336B CN201711388017.9A CN201711388017A CN108168336B CN 108168336 B CN108168336 B CN 108168336B CN 201711388017 A CN201711388017 A CN 201711388017A CN 108168336 B CN108168336 B CN 108168336B
- Authority
- CN
- China
- Prior art keywords
- water
- tank
- gas outlet
- heat recovery
- recovery system
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/08—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
- F28D7/082—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/30—Combinations with other devices, not otherwise provided for
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/28—Methods of steam generation characterised by form of heating method in boilers heated electrically
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C3/00—Other direct-contact heat-exchange apparatus
- F28C3/06—Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
- F28F21/08—Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
- F28F21/081—Heat exchange elements made from metals or metal alloys
- F28F21/085—Heat exchange elements made from metals or metal alloys from copper or copper alloys
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The invention discloses condensation water residual heat recovery system, including antifouling process system and heat recovery system, the water inlet end of antifouling process system is connected to condensate pipe, and the water outlet of antifouling process system is connected to heat recovery system；The heat recovery system includes the hot air flow device being individually connected to antifouling process system and multiple steam stream device.It can realize that external cold air, which is heated as hot-air, supplies people's use, can realize by multiple steam stream device and carry out condensed water to regenerate water vapour after suitably heating, the steaming plant for supplying outside need is used by hot air flow device.Condensation water residual heat recovery system provided by the invention, is capable of providing hot dry wind and damp and hot wind, moreover it is possible to carry out active adjusting according to demand, the hot wind of corresponding temperature and humidity is provided, structure is simple, perfect in shape and function, have in condensation water residual heat recycling field and be extremely improved, therefore is worth of widely use.
Description
Technical field
The present invention relates to heat energy recycle technical fields, are specifically related to condensation water residual heat recovery system.
Background technique
From after the industrial revolution, steam is widely used in social life；In the industrial production, steam conduct
A kind of energy that purposes is extremely wide has indivisible contact with almost all of enterprise.A large amount of industrial water and with coal
The energy based on charcoal is used to produce steam, and the heating power of steam is used to realize industrial product process procedure again, and steam is released
The condensed water produced after the thermal energy of discharge section is often drained off, and condensed water possesses a large amount of heat, typically constitutes from steam heat total amount
20%~30% or so, certain equipment may be up to 30%.
Condensed water is directly subjected to the waste that discharge results in the energy, the thermal energy for causing initial combustion resource to provide disappears in vain
Consumption；Meanwhile the condensed water of a large amount of discharge high heating values causes environment and greatly destroys and pollute.Firstly, big in condensed water
Calorimetric is underused, and is discharged into environment and is damaged to the temperature configuration of water body, soil, and the dynamic plant in water body and soil is made
The existence of object, microorganism is affected；Secondly, being discharged in condensed water rich in metallic elements and other substances such as iron, calcium, magnesium
In the process often without be easy to causeing water after condensed water is directly discharged to outside body of water and soil by special antifouling process
Body, soil eutrophication or cause the pH value of water body and soil to change, destroy the biological loop knot in raw water body and soil
Structure, it is totally unfavorable to environment.
China, which is advocated, adheres to the strategy of sustainable development during scientific technological advance, in technological innovation, economic progress
While need stringent control environmental problem, the existing energy of society is not only wasted to the discharge of condensed water at present, it is also further
Destroy ecological environment.
Therefore the problem of existing urgent need to resolve in the industrial production being become for the utilization of condensed water thermal energy.
Summary of the invention
In order to solve the above technical problems, the invention discloses condensation water residual heat recovery systems, it is intended to for industrial application
Condensed water afterwards carries out specific antifouling and decontamination processing, and the thermal energy being rich in condensed water is extracted utilization, improves the energy
Utilization rate；And the condensed water after processing carries out secondary use, gives full play to the reusing of water, reduces water resource
Waste.The present invention utilizes the transformation that the thermal energy in condensed water carries out diversified forms simultaneously, keeps the processing mode of condensed water cleverer
Living, waste heat recovery mode is more diversified.
In order to reach above-mentioned technical effect, the technical solution adopted by the present invention is that:
Condensation water residual heat recovery system, including antifouling process system and heat recovery system, the water inlet end of antifouling process system
It is connected to condensate pipe, the water outlet of antifouling process system is connected to heat recovery system.It is cold from the use equipment of hot water cyclesystem
The solidifying condensed water formed is entered after antifouling process system performs corresponding processing by condensate pipe, enters back into recuperation of heat system
System, after the heat of condensed water is largely absorbed, remaining water can be recirculated input hot water cyclesystem and use.
Specifically, the heat recovery system includes the hot air flow device being individually connected to antifouling process system and multiple steaming
Steam flow device.External cold air is passed through heat recovery system and heated by hot air flow device, by the temperature tune of cold air
It is discharged after saving the more suitable hot-air of temperature；Multiple steam stream device suitably heats the higher condensed water of temperature, then can be again
Secondary formation water vapour uses after being compressed as high-pressure water vapor.
Further, the hot air flow device includes hot-air devices and damp and hot device.
The hot-air devices include the first water collect tank, and the first water inlet and the first water outlet is arranged on the first water collect tank, the
One water inlet is connected to the water outlet of antifouling process system, and the first water outlet is connected to water return tank；Is additionally provided on first water collect tank
Heat exchanger tube is arranged in one air inlet and the first gas outlet, the first water collect tank inside, and one end of heat exchanger tube is connected to the first air inlet, heat exchange
The other end of pipe is connected to the first gas outlet, and the first blower is arranged at the first air inlet or the first gas outlet.
Further, the heat exchanger tube includes more spiral helicine branch pipes, and branch pipe uses the good metal material of thermal conductivity
Material is made.
The principle of hot-air devices are as follows: by containing high-temperature condensation water inside the first water collect tank, cool exterior air passes through the
One air inlet enters heat exchanger tube, and the air in heat exchanger tube is heated by way of heat transfer to be transported to by the first gas outlet again
Other need gas equipment.
Further, the damp and hot device includes the second water collect tank, and the second water inlet and the are arranged on the second water collect tank
Two water outlets, the second water inlet are connected to the water outlet of antifouling process system, and the second water outlet is connected to water return tank；On second water collect tank
The second air inlet and the second gas outlet are also set up, the second air inlet is communicated to the bottom of the second water collect tank, and the second gas outlet is located at
At the top of second water collect tank；Second blower is set at the second air inlet or the second gas outlet.
The principle of damp and hot device are as follows: by containing high-temperature condensation water inside the second water collect tank, cool exterior air passes through the
Two air inlets are passed into the second water collect tank, and the second air inlet is passed into the bottom of the second water collect tank, then cold air is directly logical
Enter in high-temperature condensation water and has been heated；Cold air passes through the second of the second water collect tank top after being heated in high-temperature condensation water
Gas outlet, which is transported to other, needs gas equipment.
Further, for the ease of with gas it is more convenient be suitable for, need the temperature and humidity to the air after heating to detect
And adjusting, it is equipped with the first mixed gas outlet at first gas outlet, is equipped with the second mixed gas outlet at second gas outlet, first
Mixed gas outlet and the second mixed gas outlet merge into mixed gas outlet, and the first mixed gas outlet and the second mixed gas outlet are provided with
Valve, mixed gas outlet are provided with Hygrothermograph.When there are certain requirements to the temperature and humidity of the hot-air of discharge, unlatching can be passed through
First mixed gas outlet and the second mixed gas outlet, it is defeated from the outlet of mixed gas after heated dry air and damp-heat air are mixed according to a certain percentage
Out.
The valve of first mixed gas outlet and the second mixed gas outlet is solenoid valve, and mixed gas outlet is provided with controller,
The detected value of Hygrothermograph is transported to controller, and controller is according to the mixed gas outlet of detected value regulation first and the second mixed gas outlet
The open amount of solenoid valve mixes heated dry air with damp-heat air and reaches the gas that temperature and humidity is suitble to demand.
Further, the multiple steam stream device includes third water collect tank, be arranged on third water collect tank third water inlet,
Third water outlet and steam port, third water inlet are connected to the water outlet of antifouling process system, and third water outlet is connected to water return tank, steam
Steam valve is provided at steam ports；Multiple steam stream device further includes heating device, and heating device includes being located at third water collect tank lower part
Host and the heater strip inside third water collect tank.
The principle of multiple steam stream device are as follows: by heating device electrified regulation, the condensed water in third water collect tank is made to heat up
Evaporation becomes water vapour, and water vapour is delivered to external steaming plant by steam valve, and high pressure water steaming can be formed after being pressurizeed
Vapour uses.When not needing using water vapour, multiple steam stream device, which can close, not to be had to.
Above-mentioned hot-air devices, damp and hot device and multiple steam stream device passes through the water outlet of water pipe Yu antifouling process system respectively
End connection, it is therefore intended that realize individually control, to hot-air devices, damp and hot device and multiple steam stream device needing to open or
Respective operations can be realized when closing in time.
Further, the antifouling process system includes the primary filter, deironing filter and demineralizer being sequentially communicated,
The water inlet end of antifouling process system is located on primary filter, and water outlet is located on demineralizer.
The primary filter includes that just effect filter tank, first imitate are equipped with strainer group and filtering element in filter tank.Primary filter
Effect is to remove impurity subsidiary in condensed water, preliminary purification condensed water.
Further, in order to inside whole system pressure and flow be monitored and control, the primarily efficient filter
The water inlet end of device is provided with hydraulic inductor and flowmeter, and hydraulic alarm, hydraulic inductor are additionally provided on primary filter
It is connected to hydraulic alarm.When the flow of system increases, the hydraulic of internal system is increased, in order to avoid there is system damage
It is bad and unexpected, report hydraulic alarm to be provided with hydraulic alarm preset value, when it is hydraulic reach alarm preset value when, hydraulic alarm hair
It alarms out.
Further, the deironing filter includes removing iron filter tank, except setting is equipped with catalysis oxidation in iron filter tank and magnetic is poly-
Close unit.The effect of deironing filter is that ferrous ion is able to complete oxidation under the action of catalyst, and in magnetic fields
Lower partial size becomes larger to more than micron order, is intercepted under the action of filter interior strainer by filtering.
Further, the demineralizer is Na-ion exchanger, by the container of splendid attire resin, resin, valve or conciliation
Device and control system composition, for removing the substances such as calcium ion and magnesium ion in condensed water.
Further, first water collect tank, the second water collect tank, third water collect tank, water return tank, just effect filter tank and remove iron
Sewage pipe is provided on filter tank.
Further, first water collect tank, the second water collect tank, third water collect tank, water return tank, just effect filter tank and remove iron
Inner insulating layer and thermometer are provided in filter tank.
The thermal insulation layer is coating made of heat-reflecting material.
Further, it is provided with level switch in first water collect tank, the second water collect tank or third water collect tank,
Level switch connects water level alarm.
Antifouling process system and heat recovery system and its respectively inside connection be all made of attemperater, attemperater
It is inside and outside to be coated with heat preservation reflecting layer.
Compared with prior art, the beneficial effects of the present invention are:
1. overall structure of the present invention is simple, it is convenient to realize, the waste heat of condensed water has been carried out reasonable utilization, has improved the energy
Resource is greatly saved in utilization rate.
2. hot-air devices of the invention and damp and hot device can individually provide heated dry air and damp-heat air, can also cooperate
It adjusts and the air of specific temperature and humidity demand is provided, using flexible can utilize in different environment, and compatibility is strong.
3. the present invention is also provided with multiple steam stream device, high-temperature condensation water, which can be carried out suitably heating, to be reacquired
High-temperature water vapor improves the sustainable use of condensed water.
Detailed description of the invention
In order to illustrate the technical solution of the embodiments of the present invention more clearly, below will be to needed in the embodiment attached
Figure is briefly described, it should be understood that the following drawings only shows section Example of the invention, therefore is not to be taken as pair
The restriction of range for those of ordinary skill in the art without creative efforts, can also be according to this
A little attached drawings obtain other relevant attached drawings.
Fig. 1 is composition schematic diagram of the invention.
In above-mentioned attached drawing, the corresponding title of appended drawing reference are as follows: 1- primary filter, 101- strainer group, 102- filtering element, 2- are removed
Iron filter, 3- demineralizer, the first water inlet of 4-, the first water outlet of 5-, the second water inlet of 6-, the second water outlet of 7-, 8- third
Water inlet, 9- third water outlet, the first water collect tank of 10-, the first air inlet of 1001-, the first gas outlet 1002-, 1003- heat exchange
Pipe, 1004- sewage pipe, the second water collect tank of 11-, the second air inlet of 1101-, the second gas outlet 1102-, 12- third water collect tank,
13- steam port, 14- heating device, 1401- heater strip, 15- first mix gas outlet, and 16- second mixes gas outlet, and 17- mixes gas and goes out
Mouthful.
Specific embodiment
The present invention will be further explained below with reference to the attached drawings.Embodiments of the present invention include but is not limited to following implementation
Example.
Embodiment
As shown in Figure 1, present embodiment discloses condensation water residual heat recovery system, including antifouling process system and recuperation of heat system
System, the water inlet end of antifouling process system are connected to condensate pipe, and the water outlet of antifouling process system is connected to heat recovery system.
Specifically, the heat recovery system includes the hot air flow device being individually connected to antifouling process system and multiple steaming
Steam flow device.
Hot air flow device includes hot-air devices and damp and hot device.
Hot-air devices include the first water collect tank 10, and the first water inlet 4 and the first water outlet 5 is arranged on the first water collect tank 10,
First water inlet 4 is connected to the water outlet of antifouling process system, and the first water outlet 5 is connected to water return tank；It is also set on first water collect tank 10
It is equipped with the first air inlet 1001 and the first gas outlet 1002, heat exchanger tube 1003, heat exchanger tube 1003 are set inside the first water collect tank 10
One end be connected to the first air inlet 1001, the other end of heat exchanger tube 1003 is connected to the first gas outlet 1002, the first air inlet 1001
The first blower of place's setting.
Heat exchanger tube 1003 includes more spiral helicine branch pipes, and branch pipe is made of the good metallic copper material of thermal conductivity, is propped up
The wall thickness of pipe is 0.1mm.
Damp and hot device includes the second water collect tank 11, and the second water inlet 6 and the second water outlet 7 is arranged on the second water collect tank 11,
Second water inlet 6 is connected to the water outlet of antifouling process system, and the second water outlet 7 is connected to water return tank；It is also set on second water collect tank 11
Set the second air inlet 1101 and the second gas outlet 1102, the second air inlet 1101 is communicated to the bottom of the second water collect tank 11, and second
Gas outlet 1102 is located at 11 top of the second water collect tank；Second wind is set at the second air inlet 1101 or the second gas outlet 1102
Machine.
In the present embodiment, it is helical form that the second air inlet 1101, which enters the part inside the second water collect tank 11, in this way
The meaning of setting is, can extend inside the second water collect tank of cold air 11 by the time, cold air is sufficiently heated.
For the ease of with gas it is more convenient be suitable for, need the temperature and humidity to the air after heating to be detected and adjusted, institute
It states and is equipped with the first mixed gas outlet 15 at the first gas outlet 1002, the second mixed gas outlet 16 is equipped at second gas outlet 1102,
First mixed gas outlet 15 is connected to the second mixed gas outlet 16 and merges into mixed gas outlet 17, and the first mixed gas outlet 15 and the second mixed gas go out
It is provided with valve at mouth 16, is provided with Hygrothermograph at mixed gas outlet 17.
Valve at first mixed gas outlet 15 and the second mixed gas outlet 16 is solenoid valve, is provided with control at mixed gas outlet 17
Device processed, the detected value of Hygrothermograph are transported to controller, and controller is mixed according to the mixed gas outlet 15 and second of detected value regulation first
The open amount of solenoid valve at gas outlet 16 mixes heated dry air with damp-heat air and reaches the gas that temperature and humidity is suitble to demand.
Multiple steam stream device includes third water collect tank 12, and third water inlet 8, third water outlet is arranged on third water collect tank 12
9 and steam port 13, third water inlet 8 is connected to the water outlet of antifouling process system, and third water outlet 9 is connected to water return tank, steam port
Steam valve is provided at 13；Multiple steam stream device further includes heating device 14, and heating device 14 includes being located at third water collect tank 12
The host of lower part and the heater strip 1401 inside third water collect tank 12.
Heating device 14 is electric heater unit 14, and heater strip 1401 is made of conductive copper, can be heated after energization.
Above-mentioned hot-air devices, damp and hot device and multiple steam stream device passes through the water outlet of water pipe Yu antifouling process system respectively
End is connected to, and is provided with solenoid valve on every individual water pipe, solenoid valve is connected to controller.
Antifouling process system includes the primary filter 1, deironing filter 2 and demineralizer 3 being sequentially communicated, antifouling process system
The water inlet end of system is located on primary filter 1, and water outlet is located on demineralizer 3.
Primary filter 1 includes just imitating filter tank, just imitates and is equipped with strainer group 101 and filtering element 102 in filter tank, and strainer uses 400
The three-layer metal net of mesh, 600 mesh and 800 mesh, strainer group 101 and filtering element 102 are detachable, convenient for safeguarding and replacement.
In order to inside whole system pressure and flow be monitored and control, the water inlet of the primary filter 1
End is provided with hydraulic inductor and flowmeter, and hydraulic alarm, hydraulic inductor and hydraulic report are additionally provided on primary filter 1
Alert device connection.
In the present embodiment, solenoid valve is provided at water inlet end, solenoid valve is connect with controller, and hydraulic alarm preset value
For 0.3mPa.When it is hydraulic reach hydraulic alarm preset value when, hydraulic alarm equipment alarm, controller closes the solenoid valve of water inlet end
It closes, limits going successively to for condensed water.
Deironing filter 2 includes removing iron filter tank, except setting is equipped with catalysis oxidation and magnetic polymerized unit in iron filter tank.Except iron mistake
The effect of filter 2 is that ferrous ion is able to complete oxidation under the action of catalyst, and under magnetic fields partial size become larger to
It more than micron order, is intercepted under the action of filter interior strainer by filtering.
Demineralizer 3 is Na-ion exchanger, by the container of splendid attire resin, resin, valve or demodulator and control system
Composition, for removing the substances such as calcium ion and magnesium ion in condensed water.
First water collect tank 10, third water collect tank 12, water return tank, just imitates filter tank and except equal on iron filter tank at second water collect tank 11
It is provided with sewage pipe 1004, two-way valve is set at sewage pipe 1004, opens carry out blowdown when needed；Meanwhile working as internal system
It is hydraulic excessively high, 1004 pressure release of sewage pipe can also be passed through.
First water collect tank 10, third water collect tank 12, water return tank, just imitates filter tank and except equal in iron filter tank at second water collect tank 11
It is provided with inner insulating layer and thermometer.
The thermal insulation layer is coating made of heat-reflecting material.
Meanwhile first water collect tank 10, the second water collect tank 11, third water collect tank 12, water return tank, just effect filter tank and removing iron filter tank
Outer surface be additionally provided with insulating layer, the insulating layer is made of cellular insulant.
Level switch, water level detecting are provided in first water collect tank 10, the second water collect tank 11 or third water collect tank 12
Device connects water level alarm.
Antifouling process system and heat recovery system and its respectively inside connection be all made of attemperater, attemperater
It is inside and outside to be coated with heat preservation reflecting layer.
Keeping the temperature reflecting layer is coating made of heat-reflecting material.
According to above-described embodiment, the present invention can be realized well.It is worth noting that being based on above-mentioned design principle, it is
Same technical problem is solved, even if that makes in structure basis disclosed in this invention is some without substantive change or profit
Color, used technical solution essence is still as the present invention, therefore it should also be as within the scope of the present invention.
Claims (10)
1. the water inlet end of condensation water residual heat recovery system, including antifouling process system and heat recovery system, antifouling process system connects
It is connected to condensate pipe, the water outlet of antifouling process system is connected to heat recovery system；It is characterized by:
The heat recovery system includes the hot air flow device being individually connected to antifouling process system and multiple steam stream device；It is described
Hot air flow device includes hot-air devices and damp and hot device；
The hot-air devices include the first water collect tank (10), and the first water inlet (4) and first is arranged on the first water collect tank (10) and goes out
The mouth of a river (5), the first water inlet (4) are connected to the water outlet of antifouling process system, and the first water outlet (5) is connected to water return tank；First collection
The first air inlet (1001) and the first gas outlet (1002) are additionally provided on water pot (10), setting is changed inside the first water collect tank (10)
Heat pipe (1003), one end of heat exchanger tube (1003) are connected to the first air inlet (1001), the other end connection of heat exchanger tube (1003) the
The first blower is arranged at the first air inlet (1001) or the first gas outlet (1002) for one gas outlet (1002)；
The damp and hot device includes the second water collect tank (11), and the second water inlet (6) and second is arranged on the second water collect tank (11)
Water outlet (7), the second water inlet (6) are connected to the water outlet of antifouling process system, and the second water outlet (7) is connected to water return tank；Second
The second air inlet (1101) and the second gas outlet (1102) are also set up on water collect tank (11), the second air inlet (1101) is communicated to
The bottom of two water collect tanks (11), the second gas outlet (1102) are located at the top of the second water collect tank (11)；Second air inlet (1101) or
Second blower is set at the second gas outlet of person (1102)；
The multiple steam stream device includes third water collect tank (12), and third water inlet (8), the are arranged on third water collect tank (12)
Three water outlets (9) and steam port (13), third water inlet (8) are connected to the water outlet of antifouling process system, and third water outlet (9) is even
Logical water return tank, steam port are provided with steam valve at (13)；Multiple steam stream device further includes heating device (14), heating device (14)
Including being located at the host of third water collect tank (12) lower part and being located at third water collect tank (12) internal heater strip (1401).
2. condensation water residual heat recovery system according to claim 1, which is characterized in that the antifouling process system include according to
Primary filter (1), deironing filter (2) and the demineralizer (3) of secondary connection, the water inlet end of antifouling process system, which is located at, just imitated
On filter (1), water outlet is located on demineralizer (3).
3. condensation water residual heat recovery system according to claim 2, which is characterized in that primary filter (1) packet
It includes and just imitates filter tank, just imitate and be equipped with strainer group (101) and filtering element (102) in filter tank.
4. condensation water residual heat recovery system according to claim 2, which is characterized in that the primary filter (1)
Water inlet end is provided with hydraulic inductor and flowmeter, is additionally provided with hydraulic alarm on primary filter (1), hydraulic inductor with
Hydraulic alarm connection.
5. condensation water residual heat recovery system according to claim 3, which is characterized in that the deironing filter (2) includes
Except iron filter tank, except setting is equipped with catalysis oxidation and magnetic polymerized unit in iron filter tank.
6. condensation water residual heat recovery system according to claim 1, which is characterized in that the heat exchanger tube (1003) includes
More spiral helicine branch pipes, branch pipe are made of the good metal material of thermal conductivity.
7. condensation water residual heat recovery system according to claim 5, which is characterized in that first water collect tank (10),
Second water collect tank (11), third water collect tank (12), water return tank, just effect filter tank and except being provided with sewage pipe on iron filter tank
(1004).
8. condensation water residual heat recovery system according to claim 1, which is characterized in that at first gas outlet (1002)
Equipped with the first mixed gas outlet (15), the second mixed gas outlet (16), the first mixed gas outlet are equipped at second gas outlet (1102)
(15) it is connected to the second mixed gas outlet (16) and merges into mixed gas outlet (17), the first mixed gas outlet (15) and the second mixed gas outlet
(16) it is provided with valve at, is provided with Hygrothermograph at mixed gas outlet (17).
9. condensation water residual heat recovery system according to claim 5, which is characterized in that first water collect tank (10),
Second water collect tank (11), third water collect tank (12), water return tank, just effect filter tank and except being provided with inner insulating layer and temperature in iron filter tank
Degree meter.
10. condensation water residual heat recovery system according to claim 1, which is characterized in that first water collect tank (10),
Level switch is provided in second water collect tank (11) or third water collect tank (12), level switch connects water level alarm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711388017.9A CN108168336B (en) | 2017-12-20 | 2017-12-20 | Condensation water residual heat recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711388017.9A CN108168336B (en) | 2017-12-20 | 2017-12-20 | Condensation water residual heat recovery system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108168336A CN108168336A (en) | 2018-06-15 |
| CN108168336B true CN108168336B (en) | 2019-08-27 |
Family
ID=62523260
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711388017.9A Active CN108168336B (en) | 2017-12-20 | 2017-12-20 | Condensation water residual heat recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108168336B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1562000A1 (en) * | 2004-02-03 | 2005-08-10 | Gerhard Dr. Luther | Recovering of waste heat of fumes of a heat generator |
| CN101852514A (en) * | 2010-06-02 | 2010-10-06 | 周少瑛 | Heat energy exchange unit |
| CN202581244U (en) * | 2012-02-29 | 2012-12-05 | 江苏太阳宝新能源有限公司 | Molten salt steam generation device for solar photo-thermal power generation |
| CN104843896A (en) * | 2014-12-03 | 2015-08-19 | 重庆摩尔水处理设备有限公司 | Filter for removing iron from condensed water |
| CN205773864U (en) * | 2016-06-15 | 2016-12-07 | 潍坊汇胜绝缘技术有限公司 | A kind of cooling circulating water recycling system |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201302400Y (en) * | 2008-11-14 | 2009-09-02 | 陈瑞刚 | A multifunctional modular condensed water absorption heat-exchange machine set |
| US20110083620A1 (en) * | 2009-10-08 | 2011-04-14 | Yoon Yong K | Waste Heat Recovery System and Method Thereof |
| CN103727700A (en) * | 2014-01-06 | 2014-04-16 | 杭州沃润节能科技有限公司 | Waste heat recovering system aiming at discontinuous and impure waste water resources |
| CN204372904U (en) * | 2014-11-25 | 2015-06-03 | 河南中烟工业有限责任公司 | The boiler deironing water supply part of steam utilization condensation water recovery system |
| CN205664356U (en) * | 2016-06-02 | 2016-10-26 | 白银中天化工有限责任公司 | Comdenstion water circulation recycle device |
-
2017
- 2017-12-20 CN CN201711388017.9A patent/CN108168336B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1562000A1 (en) * | 2004-02-03 | 2005-08-10 | Gerhard Dr. Luther | Recovering of waste heat of fumes of a heat generator |
| CN101852514A (en) * | 2010-06-02 | 2010-10-06 | 周少瑛 | Heat energy exchange unit |
| CN202581244U (en) * | 2012-02-29 | 2012-12-05 | 江苏太阳宝新能源有限公司 | Molten salt steam generation device for solar photo-thermal power generation |
| CN104843896A (en) * | 2014-12-03 | 2015-08-19 | 重庆摩尔水处理设备有限公司 | Filter for removing iron from condensed water |
| CN205773864U (en) * | 2016-06-15 | 2016-12-07 | 潍坊汇胜绝缘技术有限公司 | A kind of cooling circulating water recycling system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108168336A (en) | 2018-06-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103615754B (en) | Intelligent movable heat storage and supply device with steam heating function | |
| CN101603785B (en) | Heat exchange water recoverer for waste steam of steaming cabinet and external connection structure thereof | |
| CN105662130B (en) | Steaming equipment is recycled in a kind of steam pressure, temperature-controllable thermal energy | |
| CN203058203U (en) | Evaporated steam recovery recycling equipment system | |
| CN108168336B (en) | Condensation water residual heat recovery system | |
| CN206915976U (en) | A kind of sewage source heat pump and equipment associated with sludge drying | |
| CN207161279U (en) | A kind of energy-saving steam waste heat recovery device | |
| CN202717683U (en) | Sludge drying device | |
| CN108225001A (en) | Marine environment is prepared and heat pump drying integrated apparatus with fresh water | |
| CN108467017A (en) | A kind of sulfur dioxide gasification process for thionyl chloride production | |
| CN108928983A (en) | A kind of sewage low temperature distillation processing system | |
| CN201488608U (en) | Steam cabinet exhaust steam water heat exchange recoverer and external connecting structure thereof | |
| CN211233839U (en) | Dry heat recovery equipment and system | |
| CN100451190C (en) | Efficient energy-saving device of heating-gas circulation use for producing carbon fiber | |
| CN203959979U (en) | A kind ofly utilize the solar powered energy-conservation water system of making | |
| CN208980510U (en) | A kind of sewage low temperature distillation processing system | |
| CN207918433U (en) | A kind of concentration systems of recycling dilute sulfuric acid | |
| CN204251352U (en) | A kind of exhaust steam of aluminum oxide production process utilizes device | |
| CN207546157U (en) | The waste heat from tail gas recycling of lithium ferric manganese phosphate and cleaning system | |
| CN203798205U (en) | Industrial waste gas waste heat-recycling heat exchanging device | |
| CN208186295U (en) | A kind of composite heat transfer high efficiency steam generator | |
| CN207514987U (en) | A kind of vertical energy-saving microwave boiler | |
| CN207294478U (en) | New type high temperature effluent treatment plant and system | |
| CN202415205U (en) | Treating system for nanofiltration concentrated liquor of landfill leachate | |
| CN215530969U (en) | Be used for aquaculture hydrothermal circulating device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |