CN108168336A - Condensation water residual heat recovery system - Google Patents
Condensation water residual heat recovery system Download PDFInfo
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- CN108168336A CN108168336A CN201711388017.9A CN201711388017A CN108168336A CN 108168336 A CN108168336 A CN 108168336A CN 201711388017 A CN201711388017 A CN 201711388017A CN 108168336 A CN108168336 A CN 108168336A
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- water
- tank
- heat recovery
- gas outlet
- recovery system
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Classifications
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- 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
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- 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
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- 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
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- 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
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- 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 systems, and including antifouling process system and heat recovery system, the water inlet end of antifouling process system is connected to condensate pipe, the water outlet connection heat recovery system of antifouling process system；The heat recovery system includes the hot air flow device individually connected with antifouling process system and multiple steam stream device.It can realize that external cold air 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 humiture, simple in structure, perfect in shape and function are provided, have in condensation water residual heat recycling field and be extremely improved, therefore be worth of widely use.
Description
Technical field
The present invention relates to heat energy recycle technical field, more particularly to condensation water residual heat recovery system.
Background technology
From after the industrial revolution, steam is widely used in social life；In the industrial production, steam conduct
A kind of extremely wide energy of purposes 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
It releases the condensed water produced after partial heat energy to be often drained off, 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%.
Directly condensed water is carried out to discharge the waste for resulting in the energy, the thermal energy that initial combustion resource provides is caused to disappear in vain
Consumption；Meanwhile the condensed water of a large amount of discharge high heating values causes environment and greatly destroys and pollute.First, it is big in condensed water
Calorimetric is underused, and is discharged into environment and the temperature configuration of water body, soil is damaged, and makes the dynamic plant in water body and soil
The existence of object, microorganism is affected；Secondly, it is being discharged in condensed water rich in metallic elements and other substances such as iron, calcium, magnesium
In the process often after condensed water is directly discharged to outside body of water and soil, water is be easy to cause without passing through special antifouling process
Body, soil eutrophication or the acid-base value of water body and soil is caused to change, destroy the biological loop knot in raw water body and soil
Structure, it is totally unfavorable to environment.
China 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.
Invention content
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 thermal energy in condensed water is carried out the transformation utilization of diversified forms by the present invention simultaneously, and the processing mode for making condensed water is cleverer
Living, waste heat recovery mode is more diversified.
In order to reach above-mentioned technique effect, the technical solution adopted by the present invention is：
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 connection heat recovery system of antifouling process system.It is cold from the use equipment of hot water cyclesystem
The solidifying condensed water formed enters antifouling process system by condensate pipe and carries out after processing accordingly, enters back into recuperation of heat system
System, by after a large amount of absorb, remaining water can be recirculated input hot water cyclesystem and use the heat of condensed water.
Specifically, the heat recovery system includes the hot air flow device individually connected with 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 are set on the first water collect tank, the
One water inlet connects the water outlet of antifouling process system, the first water outlet connection water return tank；Is additionally provided on first water collect tank
One air inlet and the first gas outlet, the first water collect tank inside setting heat exchanger tube, one end of heat exchanger tube connect the first air inlet, heat exchange
The other end of pipe connects the first gas outlet, and the first wind turbine is set 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 is：By containing high-temperature condensation water inside the first water collect tank, cool exterior air passes through
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 again by the first gas outlet
Other need gas equipment.
Further, the damp and hot device includes the second water collect tank, and the second water inlet and the are set on the second water collect tank
Two water outlets, the second water inlet connect the water outlet of antifouling process system, the second water outlet connection 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 wind turbine is set at the second air inlet or the second gas outlet.
The principle of damp and hot device is：By containing high-temperature condensation water inside the second water collect tank, cool exterior air passes through
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 heated；Cold air heated in high-temperature condensation water after by the second of the second water collect tank top
Gas outlet, which is transported to other, needs gas equipment.
Further, it for the ease of more convenient suitable with gas, needs to be detected the humiture of the air after heating
And adjusting, the first mixed gas outlet is equipped 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 both provided with
Valve, mixed gas outlet are provided with Hygrothermograph.When there are certain requirements to the humiture 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
Go 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 first mixed gas outlet of detected value regulation and control and the second mixed gas outlet
The open amount of solenoid valve makes heated dry air be mixed with damp-heat air and reaches the gas that humiture is suitble to demand.
Further, the multiple steam stream device includes third water collect tank, setting third water inlet on third water collect tank,
Third water outlet and steam port, third water inlet connect the water outlet of antifouling process system, and third water outlet connection water return tank is steamed
Steam valve is provided at steam ports；Multiple steam stream device further includes heating unit, and heating unit includes being located at third water collect tank lower part
Host and the heater strip inside third water collect tank.
The principle of steam stream device is again：By heating unit 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 to 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 and 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 during closing in time.
Further, the antifouling process system includes the primary filter, the deironing filter that are sequentially communicated, antifouling process
The water inlet end of system is located on primary filter, and water outlet is located on deironing filter.
The primary filter includes just effect filter tank, just imitates and strainer group and filtering element are equipped in filter tank.Primary filter
Effect is to remove impurity subsidiary in condensed water, preliminary purification condensed water.
Further, in order to which the pressure inside whole system and flow are monitored and are controlled, the primarily efficient filter
The water inlet end of device is provided with hydraulic pressure inductor and flowmeter, and primary filter Shanghai is provided with hydraulic pressure alarm, hydraulic pressure inductor
It is connected with hydraulic pressure alarm.When the flow increase of system, the hydraulic pressure of internal system increases, in order to avoid there is system damage
Bad and unexpected, report hydraulic pressure alarm is provided with hydraulic pressure alarm preset value, when hydraulic pressure reaches alarm preset value, hydraulic pressure alarm hair
Go out alarm.
Further, the deironing filter is included except iron filter tank, except setting gathers equipped with catalysis oxidation and magnetic in iron filter tank
Close unit.The effect of deironing filter is that ferrous ion is able to complete oxidation under catalyst action, and in magnetic fields
Lower grain size becomes larger to more than micron order, is intercepted under the action of filter interior strainer by filtering.
Further, first water collect tank, the second water collect tank, third water collect tank, just water return tank, effect filter tank and except iron
Blow-off pipe is both provided on filter tank.
Further, first water collect tank, the second water collect tank, third water collect tank, just water return tank, effect filter tank and except iron
Inner insulating layer and thermometer are both provided in filter tank.
The thermal insulation layer is coating made of heat-reflecting material.
Further, level switch is provided 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 internal connection uses 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. the hot-air devices and damp and hot device of the present invention can individually provide heated dry air and damp-heat air, can also coordinate
The air that specific humiture demand is provided is adjusted, 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.
Description of the drawings
It 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 the section Example of the present 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 the composition schematic diagram of the present invention.
In above-mentioned attached drawing, reference numeral is corresponding entitled：1- primary filters, 101- strainer groups, 102- filtering elements, 2- are removed
Iron filter, the first water inlets of 4-, the first water outlets of 5-, the second water inlets of 6-, the second water outlets of 7-, 8- third water inlets, 9-
Third water outlet, the first water collect tanks of 10-, the first air inlets of 1001-, the first gas outlets of 1002-, 1003- heat exchanger tubes, 1004- rows
Dirt pipe, the second water collect tanks of 11-, the second air inlets of 1101-, the second gas outlets of 1102-, 12- third water collect tanks, 13- steam ports,
14- heating units, 1401- heater strips, 15- first mix gas outlet, and 16- second mixes gas outlet, and 17- mixes gas outlet.
Specific embodiment
The invention will be further described below in conjunction with the accompanying drawings.Embodiments of the present invention include but 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, the water outlet connection heat recovery system of antifouling process system.
Specifically, the heat recovery system includes the hot air flow device individually connected with 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 are set on the first water collect tank 10,
First water inlet 4 connects the water outlet of antifouling process system, the first water outlet 5 connection 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 1002,10 inside setting heat exchanger tube 1003 of the first water collect tank, heat exchanger tube 1003
One end connect the first air inlet 1001, the other end of heat exchanger tube 1003 connects the first gas outlet 1002, the first air inlet 1001
The first wind turbine 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, props 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 are set on the second water collect tank 11,
Second water inlet 6 connects the water outlet of antifouling process system, the second water outlet 7 connection water return tank；It is also set on second water collect tank 11
Put 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, the second air inlet 1101 enters the part inside the second water collect tank 11 as helical form, 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 fully heated.
For the ease of more convenient suitable with gas, need that the humiture of the air after heating is detected and adjusted, institute
It states and the first mixed gas outlet 1715 is equipped at the first gas outlet 1002, the second mixed gas outlet is equipped at second gas outlet 1102
1716, the first mixed gas outlet 1715 connects with the second mixed gas outlet 1716 and merges into mixed gas outlet 17, the first mixed gas outlet 1715
Valve is both provided with at the second mixed gas outlet 1716, Hygrothermograph is provided at mixed gas outlet 17.
Valve at first mixed 1715 and second mixed gas outlet 1716 of gas outlet is solenoid valve, mixes and is set at gas outlet 17
There is controller, the detected value of Hygrothermograph is transported to controller, and controller exports 1715 Hes according to the first mixed gas of detected value regulation and control
The open amount of solenoid valve at second mixed gas outlet 1716 makes heated dry air be mixed with damp-heat air and reaches humiture and be suitble to demand
Gas.
Multiple steam stream device includes third water collect tank 12, and third water inlet 8, third water outlet are set on third water collect tank 12
9 and steam port 13, third water inlet 8 connects the water outlet of antifouling process system, and third water outlet 9 connects water return tank, steam port
Steam valve is provided at 13；Multiple steam stream device further includes heating unit 14, and heating unit 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 unit 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 and antifouling process system respectively
End connects, 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, the deironing filter 2 that are sequentially communicated, the water inlet of antifouling process system
End is located on primary filter 1, and water outlet is located on deironing filter 2.
Primary filter 1 includes just effect filter tank, just imitates and strainer group 101 and filtering element 102 are equipped 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 replacing.
In order to which the pressure inside whole system and flow are monitored and are controlled, the water inlet of the primary filter 1
End is provided with hydraulic pressure inductor and flowmeter, and 1 Shanghai of primary filter is provided with hydraulic pressure alarm, hydraulic pressure inductor and hydraulic pressure report
Alert device connection.
In the present embodiment, solenoid valve is provided at water inlet end, solenoid valve is connect with controller, and hydraulic pressure alarm preset value
For 0.3mPa.When hydraulic pressure reaches hydraulic pressure alarm preset value, hydraulic pressure alarm equipment alarm, controller closes the solenoid valve of water inlet end
It closes, limits going successively to for condensed water.
Deironing filter 2 is included except 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, ferrous ion is able to complete oxidation under catalyst action, and under magnetic fields grain size become larger to
It more than micron order, is intercepted under the action of filter interior strainer by filtering.
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
Blow-off pipe 1004 is provided with, two-way valve is set at blow-off pipe 1004, opens carry out blowdown when needed；Meanwhile work as internal system
Hydraulic pressure it is excessively high, 1004 pressure release of blow-off 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, just water return tank, effect filter tank and except 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 internal connection uses attemperater, attemperater
It is inside and outside to be coated with heat preservation reflecting layer.
Heat preservation reflecting layer is coating made of heat-reflecting material.
According to above-described embodiment, the present invention can be realized well.What deserves to be explained is based on above-mentioned design principle, it is
The technical issues of similary is solved, even if some made on architecture basics disclosed in this invention are 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. condensation water residual heat recovery system, including antifouling process system and heat recovery system, the water inlet end of antifouling process system connects
It is connected to condensate pipe, the water outlet connection heat recovery system of antifouling process system；It is characterized in that：
The heat recovery system includes the hot air flow device individually connected with 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), the first water inlet (4) and first are set to go out on the first water collect tank (10)
The mouth of a river (5), the first water inlet (4) connect the water outlet of antifouling process system, the first water outlet (5) connection water return tank；First collection
The first air inlet (1001) and the first gas outlet (1002) are additionally provided on water pot (10), sets and changes inside the first water collect tank (10)
Heat pipe (1003), one end of heat exchanger tube (1003) connect the first air inlet (1001), the other end connection of heat exchanger tube (1003) the
One gas outlet (1002) sets the first wind turbine at the first air inlet (1001) or the first gas outlet (1002)；
The damp and hot device includes the second water collect tank (11), and the second water inlet (6) and second are set on the second water collect tank (11)
Water outlet (7), the second water inlet (6) connect the water outlet of antifouling process system, the second water outlet (7) connection 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 at the top of the second water collect tank (11)；Second air inlet (1101) or
Second wind turbine is set at the second gas outlet of person (1102)；
The multiple steam stream device includes third water collect tank (12), setting third water inlet (8) on third water collect tank (12), the
Three water outlets (9) and steam port (13), third water inlet (8) connect 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 unit (14), heating unit (14)
Including being located at the host of third water collect tank (12) lower part and positioned at the internal heater strip (1401) of third water collect tank (12).
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), the deironing filter (2) of secondary connection, the water inlet end of antifouling process system are located on primary filter (1),
Water outlet is located on deironing filter (2).
3. condensation water residual heat recovery system according to claim 2, which is characterized in that primary filter (1) packet
Just effect filter tank is included, just imitates and strainer group (101) and filtering element (102) is equipped 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 pressure inductor and flowmeter, and primary filter (1) Shanghai is provided with hydraulic pressure alarm, hydraulic pressure inductor with
Hydraulic pressure alarm connects.
5. condensation water residual heat recovery system according to claim 2, 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 1, which is characterized in that first water collect tank (10),
Second water collect tank (11), third water collect tank (12), just water return tank, effect filter tank and except being both provided with blow-off 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)
The second mixed gas, which is equipped with, equipped with the first mixed gas outlet (17) (15), at second gas outlet (1102) exports (17) (16), first
Mixed gas outlet (17) (15) connects with the second mixed gas outlet (17) (16) and merges into mixed gas outlet (17), the first mixed gas outlet (17)
(15) and at the second mixed gas outlet (17) (16) valve is both provided with, Hygrothermograph is provided at mixed gas outlet (17).
9. condensation water residual heat recovery system according to claim 1, which is characterized in that first water collect tank (10),
Second water collect tank (11), third water collect tank (12), just water return tank, effect filter tank and except being both 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, level switch connection water level alarm are provided in second water collect tank (11) or third water collect tank (12).
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 |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711388017.9A CN108168336B (en) | 2017-12-20 | 2017-12-20 | Condensation water residual heat recovery system |
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| CN108168336A true CN108168336A (en) | 2018-06-15 |
| CN108168336B CN108168336B (en) | 2019-08-27 |
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Citations (10)
| 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 |
| CN201302400Y (en) * | 2008-11-14 | 2009-09-02 | 陈瑞刚 | A multifunctional modular condensed water absorption heat-exchange machine set |
| CN101852514A (en) * | 2010-06-02 | 2010-10-06 | 周少瑛 | Heat energy exchange unit |
| US20110083620A1 (en) * | 2009-10-08 | 2011-04-14 | Yoon Yong K | Waste Heat Recovery System and Method Thereof |
| 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 |
| 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 |
| 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 |
| 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 |
| 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 |
-
2017
- 2017-12-20 CN CN201711388017.9A patent/CN108168336B/en active Active
Patent Citations (10)
| 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 |
| 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 |
| 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 |
| 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 |
| 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 |
| 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 |
| 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 |
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| CN108168336B (en) | 2019-08-27 |
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