CN101520205A - Separable heat pipe heating system - Google Patents
Separable heat pipe heating system Download PDFInfo
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- CN101520205A CN101520205A CN200910081969A CN200910081969A CN101520205A CN 101520205 A CN101520205 A CN 101520205A CN 200910081969 A CN200910081969 A CN 200910081969A CN 200910081969 A CN200910081969 A CN 200910081969A CN 101520205 A CN101520205 A CN 101520205A
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- heat pipe
- thermal source
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
Abstract
The invention relates to a separable heat pipe heating system which is characterized by comprising a heat source heat-exchange loop, an evaporation-section heat exchanger, a separable heat pipe loop and a temperature control system. The heat source heat-exchange loop is a close circulation system formed by a heat source and a heat source transfer pipeline; the separable heat pipe loop is a close circulation system formed by a multilevel condensing-section heat exchanger, a steam transfer pipeline and a low-temperature concreting pipeline, and a certain quality of phase change working substance is filled in the separable heat pipe loop; the evaporation-section heat exchanger is arranged between the heat source heat-exchange loop and the separable heat pipe loop, and the evaporation-section heat exchanger is placed lower than the condensing-section heat exchanger; the temperature control system comprises a PID controller which is connected with an automatic valve and a temperature sensor, wherein the automatic valve is mounted on the heat source transfer pipeline, and the temperature sensor is mounted on the condensing-section heat exchanger. The invention can be widely applied to places like families, factories, marketplaces, and the like where centralized heating is not available so separate heating is needed; and the invention has great economic and market foreground.
Description
Technical field
The present invention relates to a kind of heating heat-collecting system, particularly about a kind of separable heat pipe heating system that can be used in the heating systems such as family, factory and market.
Background technology
In recent years, the heating facility in city was basically towards centralized heating development, but for the family that small part in the city and rural area major part can't realize centralized heating, how to realize that more abundant effective heating is a problem demanding prompt solution.Equally, energy-saving and emission-reduction have become the common problem of paying close attention to of the whole society now, especially can produce huge thermal loss in industrial production, and how can make full use of this part low taste heat that scatters and disappears also is problem demanding prompt solution.
Compare with other heat exchanger, the heat exchange of heat pipe that with the heat pipe is heat exchange element has obvious superiority, for example heat transfer efficiency height, heat pipe surface temperature evenly, can realize that solid and solid or solid do not mix and help controlling advantages such as dew point corrosion with heat transfer, cold fluid and hot fluid between fluid, some industries at home, universal day by day as the application in the industry such as power, chemical industry, building materials and metallurgy.But because present heat pipe mainly is single tube or finned single tube structure, finishing inner phase-change liquid steam in single tube rises mobile mobile with liquid decline, this just brings, and rising flows and descend is flowing in pipe interior flow disturbance, the flowing velocity that influences each other and flowing heat transfer process.Separate heat pipe has solved steam effectively and has risen mobile and the mobile interactional process of liquid decline, and can realize remotely transferring, realize the heat exchange between a kind of fluid and multiple fluid, has excellent sealing performance, significantly adjust the area ratio of evaporator section and condensation segment, cold fluid and hot fluid is separated fully, be applicable to advantages such as heat-exchanger rig maximization.Same present separate heat pipe system mainly still adopts the structure of single hose, and it is optimum that the effect of heat exchange does not reach.
Summary of the invention
At the problems referred to above, the objective of the invention is to propose a kind of heat exchange efficiency height, simple to operate, cost is low and mount and dismount separable heat pipe heating system easily, can solve life effectively and produce in the heating needs.
For achieving the above object, the present invention takes following technical scheme: a kind of separable heat pipe heating system is characterized in that: it comprises thermal source heat-exchanging loop, evaporator section heat exchanger, detachable heat pipe circuit and temperature control system; Described thermal source heat-exchanging loop is a closed cycle system of being made up of thermal source and thermal source delivery line, described detachable heat pipe circuit is a closed cycle system of being made up of multi-stage condensing section heat exchanger, steam delivery line and cryogenic temperature condensation pipeline, and described detachable heat pipe circuit inside is injected with a certain amount of phase-change working substance; Described evaporator section heat exchanger is arranged between described thermal source heat-exchanging loop and the detachable heat pipe circuit, and described evaporator section heat exchanger placement location is lower than described condensation segment heat exchanger position; Described temperature control system comprises a PID controller, and described PID controller connects an automatic valve and a temperature sensor; Described automatic valve is installed on the described thermal source delivery line that connects between described thermal source and the evaporator section heat exchanger, and described temperature sensor is installed on the described condensation segment heat exchanger.
That described condensation segment heat exchanger in the described detachable heat pipe circuit adopts is in parallel, a kind of in series connection and the series-parallel connection arrangement, and a valve is installed on the described steam delivery line before every grade of described condensation segment heat exchanger of parallel connection, corresponding second described condensation segment heat exchanger steam inlet will be equal to or slightly lower than first described condensation segment heat exchanger steam (vapor) outlet on the described detachable heat pipe circuit of series connection, and the rest may be inferred.
Described thermal source heat-exchanging loop and described detachable heat pipe circuit are one of gas-liquid heat exchange loop and liquid liquid heat-exchanging loop.
One circulating pump is installed on the described thermal source delivery line that connects between described thermal source and the evaporator section heat exchanger in the described liquid liquid heat-exchanging loop.
Described thermal source is more than one in fire coal, combustion gas, fuel oil, solar energy and the flue gas.
Described phase-change working substance is a kind of in water, heptane, ammonia, helium, nitrogen, acetone, methyl alcohol, ethanol, freon, mercury, caesium, potassium, sodium and the lithium.
The material of described evaporator section heat exchanger and condensation segment heat exchanger is a kind of in carbon steel, low-alloy steel, stainless steel, aluminium, aluminium alloy, brass, copper, copper alloy, nickel alloy, glass, fiberglass, graphite and the polytetrafluoroethylene (PTFE).
Described steam delivery line and cryogenic temperature condensation pipeline are a kind of in metal tube and withstand voltage, corrosion resistant encapsulant metal or the flexible nonmetallic tubing.
Described evaporator section heat exchanger is a kind of in plate-fin, fin tube type, removable board-like, whole board-like, tubulation shell-and-tube and the radiator, and described condensation segment heat exchanger is more than one in plate-fin, fin tube type, removable board-like, whole board-like, tubulation shell-and-tube and the radiator.
The present invention is owing to take above technical scheme, and it has the following advantages: 1, the present invention adopts the detachable heat pipe circuit that unidirectional phase-change working substance flows to, and phase-change working substance does not have the phase mutual interference in the pipe, and flowing velocity is accelerated, and heat exchange efficiency improves greatly.2, the present invention is arranged on and is provided with a temperature control system of being made up of automatic valve, PID controller and temperature sensor between thermal source heat-exchanging loop and the detachable heat pipe circuit, temperature sensor is by the temperature of testing environment, data are regularly passed to the PID controller regulate the thermal cycle amount of the aperture of automatic valve with the control thermal source, thereby regulate the heat exchange amount effectively, make indoor temperature be stabilized in a more suitable value, realized the automatic adjusting of temperature, convenient reliable.3, the condensation segment heat exchanger in the detachable heat pipe circuit of the present invention can adopt the arrangement of parallel connection, series connection and series-parallel connection, and the number of condensation segment heat exchanger series connection can be determined according to the actual conditions in heating place in the progression of condensation segment heat exchanger parallel connection and every grade, not only increase area of dissipation effectively, and realized the heat exchange of different location, diverse location.One valve is installed on the steam delivery line before every grade of condensation segment heat exchanger of parallel connection simultaneously, by valve can also steam regulation flow, thereby realize the difference of every grade of heat exchange amount, control the temperature in the room effectively, embodied more humane advantage.4, thermal source of the present invention comprises the form of ownership of fire coal, combustion gas, fuel oil and solar energy and electrical heating, also comprise simultaneously the fume afterheat that various boilers in the industry, heating furnace, combustion furnace, smelting furnace, gas burner, thermal device produce, have thermal source source formation very widely.5, evaporator section heat exchanger of the present invention and condensation segment heat exchanger adopt the high compact heat exchange structures of the coefficient of heat transfer such as plate-fin, fin tube type, removable board-like, whole board-like, tubulation shell-and-tube or radiator, compare with common pipe and not only to have improved heat exchange efficiency greatly, and compact conformation, reduce the size of heat exchanger effectively, be convenient to installation and removal.The evaporator section heat exchanger can adopt identical heat exchange structure with the condensation segment heat exchanger simultaneously, also can adopt heat exchange structure inequality, especially for the many condensation segment heat exchangers of quantity, can adopt varying number and multi-form heat exchanger combination form according to actual conditions, so versatility is extremely strong.The present invention can be widely used in carrying out central heating and need to carry out places such as the family of individual heating, factory and market simultaneously, has very large economy and market prospects.
Description of drawings
Fig. 1 is that the present invention is not with the structural representation of water circulating pump
Fig. 2 has the structural representation of water circulating pump for the present invention
Fig. 3 is the structural representation of the embodiment of the invention 1
Fig. 4 is the structural representation of the embodiment of the invention 2
Fig. 5 is the structural representation of the embodiment of the invention 3
Fig. 6 is the structural representation of the embodiment of the invention 4
Fig. 7 is the structural representation of the embodiment of the invention 5
Fig. 8 is the structural representation of the embodiment of the invention 6
Fig. 9 is the structural representation of the embodiment of the invention 7
Figure 10 is the structural representation of the embodiment of the invention 8
Figure 11 is the structural representation of the embodiment of the invention 9
Figure 12 is the structural representation of the embodiment of the invention 10
The specific embodiment
Below in conjunction with drawings and Examples the present invention is described in detail.
As shown in Figure 1, the present invention includes thermal source heat-exchanging loop 1, evaporator section heat exchanger 2, detachable heat pipe circuit 3 and temperature control system 4.Thermal source heat-exchanging loop 1 is a closed cycle system of being made up of thermal source 11 and thermal source delivery line 12, detachable heat pipe circuit 3 is a closed cycle system of being made up of multi-stage condensing section heat exchanger 31, steam delivery line 32 and cryogenic temperature condensation pipeline 33, and detachable heat pipe circuit 3 inside are injected with a certain amount of phase-change working substance.Evaporator section heat exchanger 2 is arranged between thermal source heat-exchanging loop 1 and the detachable heat pipe circuit 3, and evaporator section heat exchanger 2 placement locations are lower than condensation segment heat exchanger 31 positions.Temperature control system 4 comprises a PID controller 41, and PID controller 41 connects an automatic valve 42 and a temperature sensor 43.Automatic valve 41 is installed on the thermal source delivery line 12 that connects thermal source 11 outlets and 2 imports of evaporator section heat exchanger, perhaps be installed on the thermal source delivery line 12 that connects 2 outlets of evaporator section heat exchanger and thermal source 11 imports, temperature sensor 43 is installed on the condensation segment heat exchanger 31.
The present invention vacuumized detachable heat pipe circuit 3 inside before using, inject the certain amount of fluid phase-change working substance then, thermal source 11 is with the liquid phase-change working medium of heat transferred evaporator section heat exchanger 2 inside, liquid phase-change working medium absorbs the heat generating gasification and forms high-temperature steam in evaporator section heat exchanger 2, high-temperature steam enters steam delivery line 32 from the top of evaporator section heat exchanger 2 and is transported to condensation segment heat exchanger 31, high-temperature steam is condensation heat in condensation segment heat exchanger 31, heat is discharged into the demand that satisfies heating in the surrounding environment by the free convection of condensation segment heat exchanger 31, the liquid phase-change working medium that is condensed simultaneously enters cryogenic temperature condensation pipeline 33 from condensation segment heat exchanger 31 bottoms, and relies on gravity and pressure reduction to carry back evaporator section heat exchanger 2 to carry out cycle heat exchange.Meanwhile, temperature sensor 43 is by the temperature of testing environment, data are regularly passed to PID controller 41 regulate the thermal cycle amount of the aperture of automatic valve 42, thereby regulate the heat exchange amount effectively, make indoor temperature be stabilized in a more suitable value with control thermal source 11.
In the foregoing description, condensation segment heat exchanger 31 in the detachable heat pipe circuit 3 can adopt the arrangement of parallel connection, series connection and series-parallel connection, and a valve 5 is installed on the steam delivery line 33 before every grade of condensation segment heat exchanger 31 of parallel connection, corresponding second condensation segment heat exchanger 31 steam inlet will be equal to or slightly lower than first condensation segment heat exchanger 31 steam (vapor) outlets on every grade of condensation segment heat exchanger 31 of series connection, and the rest may be inferred.The number of condensation segment heat exchanger 31 series connection can be determined according to the actual conditions in heating place in the progression of condensation segment heat exchanger 31 parallel connections and every grade, not only increased area of dissipation effectively, and has realized the heat exchange of different location, diverse location.In addition, by valve 5 can also steam regulation flow, thereby realize the difference of every grade of heat exchange amount, control the temperature in the room effectively, embodied more humane advantage.
In the foregoing description, evaporator section heat exchanger 2 can be divided into gas-liquid heat exchange and two kinds of forms of liquid liquid heat exchange according to the difference of thermal source heat exchange form.For the gas-liquid heat exchange form, the present invention left side is the gas-liquid heat exchange loop that thermal source 11 and evaporator section heat exchanger 2 are formed; For liquid liquid heat exchange form, the present invention left side is the liquid liquid heat-exchanging loop that thermal source 11 and evaporator section heat exchanger 2 are formed.Evaporator section heat exchanger 2 for liquid liquid heat exchange form, liquid medium can be finished heat exchange by self-loopa in evaporator section heat exchanger 2, the flow direction of liquid liquid heat exchange closed circuit requirement of the present invention this moment thermal source liquid medium is not necessarily from high to low, 2 imports of evaporator section heat exchanger will be lower than the liquid level of thermal source 11, rely on the gravity of thermal source liquid medium self or the heating that capillary force is realized phase-change working substance.In addition, can also be on the thermal source delivery line 12 that connects thermal source 11 outlets and 2 imports of evaporator section heat exchanger, one circulating pump 6 perhaps is installed to drive the liquid medium circulation on the thermal source delivery line 12 that connects 2 outlets of evaporator section heat exchanger and thermal source 11 imports, thermal source heat-exchanging loop 1 liquid medium circulation this moment not have the requirement fixed for the flow direction of liquid medium, does not have the requirement (as shown in Figure 2) of distance and installation position between thermal source 11 and the evaporator section heat exchanger 2 yet.
In the foregoing description, thermal source 11 comprises the form of ownership of fire coal, combustion gas, fuel oil and solar energy and electrical heating, also comprise simultaneously the fume afterheat that various boilers in the industry, heating furnace, combustion furnace, smelting furnace, gas burner, thermal device produce, have thermal source source formation very widely.For the heat exchange of thermal source 11 with evaporator section heat exchanger 2 interior liquid, both can adopt the direct form that flue gas, solar energy etc. are direct and evaporator section heat exchanger 2 carries out heat exchange, also can adopt first heating liquid media such as flue gas, fire coal, the indirect form of carrying out heat exchange again with liquid medium and evaporator section heat exchanger 2 after the heating, and also can unite for the various heat exchange modes of needs that satisfy heating and to intersect use.
In the foregoing description, employed phase-change working substance comprises water, heptane, ammonia, helium, nitrogen, acetone, methyl alcohol, ethanol, freon, mercury, caesium, potassium, sodium and lithium etc. in the detachable heat pipe circuit 3, according to the temperature difference of utilizing thermal source, adopt different phase-change working substances.
In the foregoing description, the material of evaporator section heat exchanger 2 and condensation segment heat exchanger 31 is different with system pressure according to the temperature of utilizing thermal source 11, can be carbon steel, low-alloy steel, stainless steel, aluminium, aluminium alloy, brass, copper, copper alloy, nickel alloy, glass, fiberglass, graphite or polytetrafluoroethylene (PTFE).
In the foregoing description, steam delivery line 32 and cryogenic temperature condensation pipeline 33 can adopt metal tube, also can adopt withstand voltage, corrosion resistant encapsulant metal and flexible nonmetallic tubing.
In the foregoing description, evaporator section heat exchanger 2 and condensation segment heat exchanger 31 can adopt heat exchange structures such as plate-fin (comprising snakelike flat tube plate-fin), fin tube type, removable board-like, whole board-like, tubulation shell-and-tube or radiator, compare with common pipe and have improved heat exchange efficiency greatly.Evaporator section heat exchanger 2 can adopt identical heat exchange structure with condensation segment heat exchanger 31, also can adopt heat exchange structure inequality.Especially for the many condensation segment heat exchangers 31 of quantity, can adopt varying number and multi-form heat exchanger combination form according to actual conditions, be the embodiment of heat exchanger combination form of the present invention below.
Embodiment 1:
As shown in Figure 3, evaporator section heat exchanger 2 is a plate type heat exchanger in the present embodiment, and condensation segment heat exchanger a, b, c, d are the plate type heat exchanger of gas-liquid heat exchange form.Evaporator section heat exchanger 2 is the hot junction of detachable heat pipe circuit 3, and condensation segment heat exchanger a, b, c, d are the cold junction of detachable heat pipe circuit 3, and both form closed detachable heat pipe circuit 3.Condensation segment heat exchanger a, other condensation segment heat exchangers and condensation segment heat exchanger c descend and are composed in series the part of detachable heat pipe circuit 3, and wherein the steam inlet height of second heat exchanger will be equal to or less than the steam (vapor) outlet of a heat exchanger.Condensation segment heat exchanger b, other condensation segment heat exchangers and the similar part that also is connected into detachable heat pipe circuit 3 of condensation segment heat exchanger d.Of this sort a plurality of series connection steam-return lines are formed the parallel form of detachable heat pipe circuit 3.
Embodiment 2:
As shown in Figure 4, evaporator section heat exchanger 2 is a plate type heat exchanger in the present embodiment, and condensation segment heat exchanger a, b, c, d are plate-fin heat exchanger, and the type of attachment of each heat exchanger is identical with embodiment 1.
Embodiment 3:
As shown in Figure 5, evaporator section heat exchanger 2 is a plate type heat exchanger in the present embodiment, condensation segment heat exchanger a, c are plate-fin heat exchanger, condensation segment heat exchanger b, d are plate type heat exchanger, the type of attachment of each heat exchanger is identical with embodiment 1, and the condensation segment heat exchanger of two kinds of different structure forms can exchange use arbitrarily in the serial or parallel connection loop.
Embodiment 4:
As shown in Figure 6, evaporator section heat exchanger 2 is a plate type heat exchanger in the present embodiment, condensation segment heat exchanger a is a fin-tube heat exchanger, condensation segment heat exchanger c is a plate-fin heat exchanger, condensation segment heat exchanger b, d are plate type heat exchanger, the type of attachment of each heat exchanger is identical with embodiment 1, and the condensation segment heat exchanger of three kinds of different structure forms can exchange use arbitrarily in the serial or parallel connection loop.
Embodiment 5:
As shown in Figure 7, evaporator section heat exchanger 2 is a plate type heat exchanger in the present embodiment, condensation segment heat exchanger a is a fin-tube heat exchanger, condensation segment heat exchanger b is a plate type heat exchanger, condensation segment heat exchanger c is a plate-fin heat exchanger, condensation segment heat exchanger d is the tubulation shell-and-tube heat exchanger, and the type of attachment of each heat exchanger is identical with embodiment 1, and the condensation segment heat exchanger of four kinds of different structure forms can exchange use arbitrarily in the serial or parallel connection loop.
Embodiment 6:
As shown in Figure 8, evaporator section heat exchanger 2 is a plate-fin heat exchanger in the present embodiment, and condensation segment heat exchanger a, b, c, d are plate-fin heat exchanger, and the type of attachment of each heat exchanger is identical with embodiment 1.
Embodiment 7:
As shown in Figure 9, evaporator section heat exchanger 2 is a plate-fin heat exchanger in the present embodiment, and condensation segment heat exchanger a, b, c, d are plate type heat exchanger, and the type of attachment of each heat exchanger is identical with embodiment 1.
Embodiment 8:
As shown in figure 10, evaporator section heat exchanger 2 is a plate-fin heat exchanger in the present embodiment, condensation segment heat exchanger a, c are the plate-fin heat exchanger of gas-liquid heat exchange form, condensation segment heat exchanger b, d are plate type heat exchanger, the type of attachment of each heat exchanger is identical with embodiment 1, and the condensation segment heat exchanger of two kinds of different structure forms can exchange use arbitrarily in the serial or parallel connection loop.
Embodiment 9:
Show as Figure 11, evaporator section heat exchanger 2 is a plate-fin heat exchanger in the present embodiment, condensation segment heat exchanger a is a fin-tube heat exchanger, condensation segment heat exchanger c is a plate-fin heat exchanger, condensation segment heat exchanger b, d are plate type heat exchanger, the type of attachment of each heat exchanger is identical with embodiment 1, and the condensation segment heat exchanger of three kinds of different structure forms can exchange use arbitrarily in the serial or parallel connection loop.
Embodiment 10:
As shown in figure 12, evaporator section heat exchanger 2 is a plate-fin heat exchanger in the present embodiment, condensation segment heat exchanger a is a fin-tube heat exchanger, condensation segment heat exchanger b is a plate type heat exchanger, condensation segment heat exchanger c is a plate-fin heat exchanger, condensation segment heat exchanger d is the tubulation shell-and-tube heat exchanger, and the type of attachment of each heat exchanger is identical with embodiment 1, and the condensation segment heat exchanger of four kinds of different structure forms can exchange use arbitrarily in the serial or parallel connection loop.
The present invention only describes with the foregoing description; the structure of each parts, the position is set and connects and all can change to some extent; on the basis of technical solution of the present invention; all improvement and equivalents of individual component being carried out according to the principle of the invention all should not got rid of outside protection scope of the present invention.
Claims (12)
1, a kind of separable heat pipe heating system is characterized in that: it comprises thermal source heat-exchanging loop, evaporator section heat exchanger, detachable heat pipe circuit and temperature control system;
Described thermal source heat-exchanging loop is a closed cycle system of being made up of thermal source and thermal source delivery line, described detachable heat pipe circuit is a closed cycle system of being made up of multi-stage condensing section heat exchanger, steam delivery line and cryogenic temperature condensation pipeline, and described detachable heat pipe circuit inside is injected with a certain amount of phase-change working substance; Described evaporator section heat exchanger is arranged between described thermal source heat-exchanging loop and the detachable heat pipe circuit, and described evaporator section heat exchanger placement location is lower than described condensation segment heat exchanger position;
Described temperature control system comprises a PID controller, and described PID controller connects an automatic valve and a temperature sensor; Described automatic valve is installed on the described thermal source delivery line that connects between described thermal source and the evaporator section heat exchanger, and described temperature sensor is installed on the described condensation segment heat exchanger.
2, a kind of separable heat pipe heating system as claimed in claim 1, it is characterized in that: the described condensation segment heat exchanger in the described detachable heat pipe circuit adopts a kind of in parallel, series connection and the series-parallel connection arrangement, and a valve is installed on the described steam delivery line before every grade of described condensation segment heat exchanger of parallel connection, corresponding second described condensation segment heat exchanger steam inlet will be equal to or slightly lower than first described condensation segment heat exchanger steam (vapor) outlet on the described detachable heat pipe circuit of series connection, and the rest may be inferred.
3, a kind of separable heat pipe heating system as claimed in claim 1 is characterized in that: described thermal source heat-exchanging loop and described detachable heat pipe circuit are one of gas-liquid heat exchange loop and liquid liquid heat-exchanging loop.
4, a kind of separable heat pipe heating system as claimed in claim 2 is characterized in that: described thermal source heat-exchanging loop and described detachable heat pipe circuit are one of gas-liquid heat exchange loop and liquid liquid heat-exchanging loop.
5, a kind of separable heat pipe heating system as claimed in claim 3 is characterized in that: a circulating pump is installed on the described thermal source delivery line that connects between described thermal source and the evaporator section heat exchanger in the described liquid liquid heat-exchanging loop.
6, a kind of separable heat pipe heating system as claimed in claim 4 is characterized in that: a circulating pump is installed on the described thermal source delivery line that connects between described thermal source and the evaporator section heat exchanger in the described liquid liquid heat-exchanging loop.
7, as claim 1 or 2 or 3 or 4 or 5 or 6 described a kind of separable heat pipe heating systems, it is characterized in that: described thermal source is more than one in fire coal, combustion gas, fuel oil, solar energy and the flue gas.
8, as claim 1 or 2 or 3 or 4 or 5 or 6 described a kind of separable heat pipe heating systems, it is characterized in that: described phase-change working substance is a kind of in water, heptane, ammonia, helium, nitrogen, acetone, methyl alcohol, ethanol, freon, mercury, caesium, potassium, sodium and the lithium.
9, a kind of separable heat pipe heating system as claimed in claim 7 is characterized in that: described phase-change working substance is a kind of in water, heptane, ammonia, helium, nitrogen, acetone, methyl alcohol, ethanol, freon, mercury, caesium, potassium, sodium and the lithium.
10, as the described a kind of separable heat pipe heating system of claim 1～9, it is characterized in that: the material of described evaporator section heat exchanger and condensation segment heat exchanger is a kind of in carbon steel, low-alloy steel, stainless steel, aluminium, aluminium alloy, brass, copper, copper alloy, nickel alloy, glass, fiberglass, graphite and the polytetrafluoroethylene (PTFE).
11, as the described a kind of separable heat pipe heating system of claim 1～10, it is characterized in that: described steam delivery line and cryogenic temperature condensation pipeline are a kind of in metal tube and withstand voltage, corrosion resistant encapsulant metal or the flexible nonmetallic tubing.
12, as the described a kind of separable heat pipe heating system of claim 1～11, it is characterized in that: described evaporator section heat exchanger is a kind of in plate-fin, fin tube type, removable board-like, whole board-like, tubulation shell-and-tube and the radiator, and described condensation segment heat exchanger is more than one in plate-fin, fin tube type, removable board-like, whole board-like, tubulation shell-and-tube and the radiator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910081969A CN101520205A (en) | 2009-04-10 | 2009-04-10 | Separable heat pipe heating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910081969A CN101520205A (en) | 2009-04-10 | 2009-04-10 | Separable heat pipe heating system |
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| CN101520205A true CN101520205A (en) | 2009-09-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200910081969A Pending CN101520205A (en) | 2009-04-10 | 2009-04-10 | Separable heat pipe heating system |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102213466A (en) * | 2011-04-15 | 2011-10-12 | 清华大学 | Thermal environmental control system |
| CN103502737A (en) * | 2010-12-03 | 2014-01-08 | 丹佛斯公司 | Heating system and method for heating a plurality of rooms |
| CN104845645A (en) * | 2015-04-30 | 2015-08-19 | 中冶南方工程技术有限公司 | Coke oven gas waste heat recovery system |
| CN110332839A (en) * | 2019-04-03 | 2019-10-15 | 沈阳化工大学 | One kind can energy storage glass fiber reinforced plastics product |
| CN113357722A (en) * | 2021-05-20 | 2021-09-07 | 青岛海尔空调器有限总公司 | Heating air conditioning fan and control method |
| CN113871038A (en) * | 2021-09-29 | 2021-12-31 | 南京航空航天大学 | Space nuclear power system adopting multistage heat exchange power shielding heat exchanger and circulation method |
-
2009
- 2009-04-10 CN CN200910081969A patent/CN101520205A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103502737A (en) * | 2010-12-03 | 2014-01-08 | 丹佛斯公司 | Heating system and method for heating a plurality of rooms |
| CN103502737B (en) * | 2010-12-03 | 2016-06-08 | 丹佛斯公司 | Heating system and the method for heating multiple room |
| CN102213466A (en) * | 2011-04-15 | 2011-10-12 | 清华大学 | Thermal environmental control system |
| CN102213466B (en) * | 2011-04-15 | 2013-12-11 | 清华大学 | Thermal environmental control system |
| CN104845645A (en) * | 2015-04-30 | 2015-08-19 | 中冶南方工程技术有限公司 | Coke oven gas waste heat recovery system |
| CN110332839A (en) * | 2019-04-03 | 2019-10-15 | 沈阳化工大学 | One kind can energy storage glass fiber reinforced plastics product |
| CN113357722A (en) * | 2021-05-20 | 2021-09-07 | 青岛海尔空调器有限总公司 | Heating air conditioning fan and control method |
| WO2022242165A1 (en) * | 2021-05-20 | 2022-11-24 | 青岛海尔空调器有限总公司 | Heating evaporative air cooler and control method |
| CN113871038A (en) * | 2021-09-29 | 2021-12-31 | 南京航空航天大学 | Space nuclear power system adopting multistage heat exchange power shielding heat exchanger and circulation method |
| CN113871038B (en) * | 2021-09-29 | 2023-09-26 | 南京航空航天大学 | Space nuclear power system adopting multistage heat exchange power shielding heat exchanger and circulation method |
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