CN108800092B - A kind of combustion gas evaporator of evaporation ends distribution density radial variations - Google Patents
A kind of combustion gas evaporator of evaporation ends distribution density radial variations Download PDFInfo
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- CN108800092B CN108800092B CN201810258150.0A CN201810258150A CN108800092B CN 108800092 B CN108800092 B CN 108800092B CN 201810258150 A CN201810258150 A CN 201810258150A CN 108800092 B CN108800092 B CN 108800092B
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- pipe
- vertical
- heat
- vertical pipe
- horizontal component
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B31/00—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus
- F22B31/08—Installation of heat-exchange apparatus or of means in boilers for heating air supplied for combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/02—Premix gas burners, i.e. in which gaseous fuel is mixed with combustion air upstream of the combustion zone
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details, e.g. noise reduction means
-
- 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
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The present invention provides a kind of gas steam generators, including water tank and heat pipe, the water tank includes water inlet and steam (vapor) outlet, the heat pipe includes vertical portion, horizontal component and vertical pipe, and wherein the bottom end of vertical portion is connected to horizontal component, and the horizontal component lower part is connected to multiple vertical pipes, wherein vertical pipe is the evaporation ends of heat pipe, vertical portion is the condensation end of heat pipe, and the vertical portion extend into water tank bottom, and the vertical pipe and horizontal component are arranged in gas burner;The vertical pipe be it is multiple, along the center radially outward direction of burner, the distribution density of the vertical pipe is smaller and smaller.The present invention is different by the density that vertical pipe is arranged in the different location in burner, integral heat pipe temperature to make keeps essentially identical, to improve whole heat exchange efficiency, saves material, local damage caused by non-uniform temperature is avoided, the service life of heat pipe is extended.
Description
Technical field
The present invention relates to a kind of vaporizer technology more particularly to a kind of evaporators of the heat pipe of Novel structure.
Background technique
Hot pipe technique is George Ge Luofo of U.S. Los Alamos (Los Alamos) National Laboratory in 1963
One kind of (George Grover) invention is known as the heat transfer element of " heat pipe ", it takes full advantage of heat-conduction principle and phase transformation is situated between
The heat of thermal objects is transmitted to outside heat source rapidly by the quick thermal transport property of matter through heat pipe, and the capacity of heat transmission is more than to appoint
The capacity of heat transmission of what known metal.
The industries such as aerospace, military project were widely used in front of hot pipe technique, since being introduced into radiator manufacturing, so that
People change the mentality of designing of traditional heat sinks, get rid of the list for obtaining more preferable heat dissipation effect by high air quantity motor merely
One radiating mode makes radiator obtain satisfied heat transfer effect using hot pipe technique, opens heat dissipation industry new world.At present
Heat pipe is widely used in various heat exchange equipments, including power domain, such as the UTILIZATION OF VESIDUAL HEAT IN of power plant etc..
Evaporator is the mechanical equipment for water being heated as using the thermal energy of fuel or other energy steam.Evaporator application
Field is extensive, is widely used in clothing factory, drycleaner's, restaurant, steamed bun shop, dining room, dining room, factories and miness, the places such as Bean Products Factory.At present
Evaporator be also widely used in the treatment of various diseases, be particularly applied to muscle, ligament etc. because of aging and old damage
The treatment of caused chronic disease, such as CN2167709Y patent, but at present in the prior art, such as CN2167709Y special
Benefit, because directly generating steam by heating, the vapor (steam) temperature that will lead to generation is excessively high, and will lead in the steam of generation
Excess moisture, and drug is because be that particle it is possible that will appear is deposited on lower part, effective component contains in the steam sprayed
Measure too low, and temperature is excessively high, and intelligence degree is not high in the prior art, can not carry out effective intelligent operation.
In the prior art, when heat pipe in evaporator, the shape of heat pipe affects the endotherm area of evaporation ends, because
This general evaporation ends heat absorption range is smaller, sometimes needs that multiple heat pipes are arranged in heat source to meet heat absorption demand;And
More heat pipes there are when, each heat pipe can generate the non-uniform phenomenon of heat absorption because the position in burner is different.
In view of the above-mentioned problems, the present invention is improved on the basis of invention in front, a kind of new structure is provided
Combustion gas evaporator makes full use of heat source, reduces energy consumption, improves combustion efficiency.
Summary of the invention
In view of the above-mentioned problems, the present invention is improved on the basis of invention in front, a kind of new heat pipe knot is provided
Structure evaporator, to realize making full use of for waste heat.
To achieve the goals above, technical scheme is as follows:
A kind of gas steam generator, including water tank and heat pipe, the water tank include water inlet and steam (vapor) outlet, the heat
Pipe includes vertical portion, horizontal component and vertical pipe, wherein the bottom end connection horizontal component of vertical portion, under the horizontal component
Portion is connected to multiple vertical pipes, and wherein vertical pipe is the evaporation ends of heat pipe, and vertical portion is the condensation end of heat pipe, the vertical portion
It is extend into water tank bottom, the vertical pipe and horizontal component are arranged in gas burner;The vertical pipe be it is multiple, along
The center radially outward direction of burner, the distribution density of the vertical pipe are smaller and smaller.
Preferably, along the center radially outward direction of burner, the distribution density of the vertical pipe is smaller and smaller
Amplitude constantly increase.
Preferably, direction of the horizontal component from the bottom end of vertical portion away from vertical portion extends, it is described
Vertical portion is the more pipes for extending to water tank bottom.
Preferably, the burner includes burner seat, it is fixedly installed on the burner seat for placing water tank
Stove circle, the combustion head for being equipped with several orifices is fixedly mounted in the burner seat, the bottom of the burner seat is equipped with combustion
Tracheae, the burner seat are equipped with the air outlet slit of several supply combustion head combustion adjuvants, the outside of the burner seat
Equipped with the intake adit being connected to the air outlet slit, the intake adit is equipped with air intake;The stove circle, the water tank
Bottom and the burner seat form combustion chamber, and the stove circle is hollow interlayer, and the internal layer double wall top of the stove circle is equipped with
Several return air inlets, the internal cavities of the stove circle are connected to the intake adit.
Preferably, the arc-shaped structure of stove circle.
Preferably, multiple air outlet slits are set from lower to upper part, and from the lower to the upper, the density of air outlet slit distribution
It is increasing.
Preferably, multiple air outlet slits are set from lower to upper part, and from the lower to the upper, the density of air outlet slit distribution
Increasing amplitude is continuously increased.
Preferably, multiple air outlet slits are arranged from lower to upper part, from the lower to the upper, the diameter of air outlet slit is more next
It is bigger.
Preferably, from the lower to the upper, the increasing amplitude of air outlet slit diameter is continuously increased.
The arc-shaped structure of stove circle.
Preferably, the horizontal component is flat tube structure, vertical pipe is circular tube structure.
Preferably, horizontal component is semi-circular structure, the vertical pipe surrounds the center annular Multi-layers distributing of horizontal component.
Preferably, vertical pipe is arranged in axial centerline, multilayer vertical pipe, every layer of vertical pipe are set along central axis
Axis it is identical at a distance from central axis, thus formed using horizontal component central axis as the arc structure in the center of circle.
Preferably, the outer diameter of vertical pipe is d, the distance between adjacent vertical pipe center of circle of same row is L, vertical pipe
The center of circle and adjacent row two closed on the vertical pipe center of circle constitute isosceles triangle apex angle be N, then meet claimed below:
Sin(N)=a-b*S2- c*S, wherein Ln is logarithmic function, and S=d/ (M2-M1), a, b, c is parameter, is met as follows
It is required that:
0.795<a<0.805, 0.525<b<0.535,0.895<b<0.905;
Preferably, a=0.803, b=0.529, c=0.903.
Compared with prior art, the present invention has the advantage that:
1) density that vertical pipe is arranged by the different location in burner in the present invention is different, thus the overall thermal tube temperature made
Degree keeps essentially identical, to improve whole heat exchange efficiency, saves material, avoids local damage caused by non-uniform temperature,
Extend the service life of heat pipe.
2) present invention improves the condensation end structure of the heat pipe in combustion gas evaporator, will be between adjacent condensation segment
Communicating pipe is set, can be even to avoid uneven heating between heat pipe by the way that communicating pipe is arranged, realize that the pressure between heat pipe is balanced,
Defect caused by avoiding the uneven heating between different heat pipes even.
3) present invention passes through the changing rule for being connected to distributed quantity and caliber, can guarantee in process fluid flow
Reach pressure equilibrium as soon as possible.
4) variation of the distribution density in the short transverse that the present invention passes through the air outlet slit of burner and diameter, can
Guarantee being sufficiently mixed for air and combustion gas, reaches full combustion.
5) present invention improves the structure of the evaporation ends of the heat pipe in evaporator, and the evaporation ends of heat pipe are extended to
Farther direction, in the case where not changing the condensation end volume of heat pipe, so that the endotherm area of the evaporation ends of heat pipe increases, this
Sample can expand the heat absorption range of heat pipe, and the heat of heat source distalmost end can be absorbed.Heat pipe evaporation in compared with the existing technology
End and condensation end are consistent size, while reducing the volume and occupied area of heat exchanger, so that compact-sized.
6) communicating pipe is arranged in adjacent evaporation ends in the present invention, pressure can be caused different in the heated difference of vertical pipe
In the case of, the fluid in evaporation ends that pressure can be made big quickly flows to the small evaporation ends of pressure, to keep whole pressure
Power is balanced, avoids hot-spot or supercooling.
Detailed description of the invention
Fig. 1 is steam generator first embodiment schematic diagram of the present invention.
Fig. 2 is steam generator second embodiment schematic diagram of the present invention.
Fig. 3 is heat pipe structure schematic diagram of the present invention.
Fig. 4 is schematic diagram of the Fig. 3 from bottom.
Fig. 5 is the heat pipe partial structural diagram of present invention setting communicating pipe.
Fig. 6 is steam generator 3rd embodiment schematic diagram of the present invention.
Fig. 7 is the partial enlargement mark schematic diagram of Fig. 4.
Fig. 8 is the structural schematic diagram of the present invention adjacent heat pipe setting communicating pipe.
Fig. 9 is burner structure schematic diagram of the present invention.
In figure: 1- burner seat, 2- stove circle, 3-combustion heads, 4- intake adit, the combustion chamber 5-, 7- orifice, 8- heat preservation
Material, 10- heat pipe, 111- air supply opening, 112- air outlet slit, 121- air outlet slit, 211- return air inlet, 101- vertical portion,
102- horizontal component, 103- vertical pipe, 104- round tube, 105- water tank, 106- heat source passages, 107- communicating pipe, 108- water inlet,
109- steam (vapor) outlet, 110- condenser pipe, 21 internal layer double walls.
Specific embodiment
Specific embodiments of the present invention will be described in detail with reference to the accompanying drawing.
Herein, if without specified otherwise, it is related to formula, "/" indicates that division, "×", " * " indicate multiplication.
If Fig. 1-8 discloses a kind of gas steam generator using heat pipe, the steam generator includes 105 He of water tank
Heat pipe 10, the water tank 105 include water inlet 108 and steam (vapor) outlet 109, and the heat pipe includes vertical portion 101, horizontal component
102 and vertical pipe 103, wherein the bottom end of vertical portion 101 is connected to horizontal component 102, and 102 lower part of the horizontal component connection is more
A vertical pipe 103, wherein vertical pipe 103 is the evaporation ends of heat pipe, and vertical portion 101 is the condensation end of heat pipe.The vertical portion
101 are divided to extend into 105 bottom of water tank, for the liquid in heating water tank.The vertical pipe 103 and the setting of horizontal component 102 exist
In heat source.
Evaporator of the present invention absorbs heat in operation, by vertical pipe 103 from heat source, then in vertical pipe 103
Fluid is evaporated, and enters vertical portion by horizontal component, then rejects heat to the water in water tank in vertical portion,
Fluid is condensed, and enters back into vertical pipe 103 by the effect of gravity.
Preferably, the vertical portion is flat tube structure.
Preferably, the heat pipe is at least two, be set between the vertical portion 101 of adjacent heat pipe communicating pipe.Example
As shown in Figure 7,8, communicating pipe 107 is set between the vertical portion 101 of two heat pipes adjacent to each other.It is connected to by setting
Pipe, can be even to avoid uneven heating between heat pipe, realizes that the pressure between heat pipe is balanced, avoid between different heat pipes it is heated not
Defect caused by uniformly.
Preferably, the distance between adjacent communicating pipe 107 is no from 101 lower part of vertical portion to 101 top of vertical portion
It is disconnected to increase.This purpose is in order to which more communicating pipes are arranged, because of flowing up with heat pipe vertical portion fluid, fluid is not
Disconnected heat release, with the continuous heat release of fluid, the pressure in different heat pipes is gradually decreased, therefore passes through above-mentioned setting, Neng Goubao
Card reaches pressure equilibrium as soon as possible in process fluid flow, saves material.
Preferably, the distance between adjacent communicating pipe 107 is no from 101 lower part of vertical portion to 101 top of vertical portion
Increased amplitude of breaking is increasing.It is found through experiments that, above-mentioned setting, can guarantee more excellent faster in process fluid flow
Reach pressure equilibrium.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Preferably, from 101 lower part of vertical portion to 101 top of vertical portion, the diameter of communicating pipe 107 constantly reduces.
This purpose be in order to be arranged and guarantee bigger connection area, because of flowing up with fluid, the continuous heat release of fluid, with
The continuous heat release of fluid, the pressure in different heat pipes is smaller and smaller, therefore by above-mentioned setting, can guarantee to flow in fluid
Reach pressure equilibrium in journey as soon as possible.
Preferably, from 101 lower part of vertical portion to 101 top of vertical portion, the diameter of communicating pipe 107 is ever-reduced
Amplitude is increasing.It is found through experiments that, above-mentioned setting, can guarantee more excellent in process fluid flow to reach pressure faster
It is balanced.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Preferably, as shown in Figure 1, the horizontal component 102 is from the bottom end of vertical portion 101 away from vertical portion
101 direction extends.Evaporator of the present invention is improved by the way that the structure of the evaporation ends of heat pipe is arranged, by the evaporation ends of heat pipe
Farther direction is extended to, in the case where not changing the condensation end volume of heat pipe, so that the endotherm area of the evaporation ends of heat pipe
Increase, the heat absorption range of heat pipe can be expanded in this way, the heat of heat source distalmost end can be absorbed.Heat in compared with the existing technology
Pipe evaporation ends and condensation end are consistent size, can be improved 45% or more heat exchange efficiency.Simultaneously reduce condensation end volume and
Occupied area, so that compact-sized.
Extend preferably, the horizontal component of described two heat pipes is respectively facing opposite direction.It is right by setting two
The heat pipe of title can absorb heat in different directions, meet the needs of heat exchange.
Preferably, medical fluid is arranged in the water tank.The evaporator is a kind of evaporator of drug fumigation in treating function.
Preferably, the steam generated is directly gone out from steam (vapor) outlet 109.
Alternatively, the evaporator further includes medical fluid evaporation tank, and the medical fluid evaporation tank passes through pipeline and water
Case 105 is connected to, and atomizer is arranged in the medical fluid evaporation tank, and steam (vapor) outlet is arranged in the medical fluid evaporation tank.
Drug is set in the water tank, the drug immersion in water, in use, being added in water tank by heat pipe
Hot water, by water come Heating Drug, to generate medical fluid in water tank 105.The medical fluid of generation enters medical fluid evaporation by pipeline
It in case, and is atomized in medical fluid evaporation tank, is then discharged by steam (vapor) outlet.Steam (vapor) outlet can be directly against patient's
Sick position discharge, for treating.
As shown in attached drawing 1,2, the burner includes burner seat 1, is fixedly installed on the burner seat 1 for putting
The stove circle 2 of water tank 105 is set, the combustion head 3 for being equipped with several orifices 7, the burner seat is fixedly mounted in the burner seat 1
1 bottom is equipped with the air supply opening 111 connecting with gas pipeline, and the burner seat 1 is equipped with several supply combustion heads 3
The air outlet slit 112 of combustion air, the outside of the burner seat 1 are equipped with the air duct 4 being connected to the air outlet slit 112,
4 lower end of air duct is equipped with air intake 121, and the shell of the air supply line 4 coats the burner seat 1, in this way can benefit
The air entered with the heating of burner seat 1, saves gas thermal energy.Preferably, being viewed from above, combustion head 3 is circular configuration
Several orifices 7 is arranged on combustion head 3, combustion gas can be made to reach optimal atomizing effect, so as to combustion gas energy
Full combustion, the stove circle 2 in horn-like, the oral area of the stove circle 2 be it is corresponding with the outer wall of the water tank round, can be with
It is heated evenly water tank, the temperature in fast lifting pot, the stove circle 2, the water tank and the burner seat 1 formation prevent
The combustion chamber 5 rushed down outside flame, the indoor flame that makes to burn avoid thermal-flame and take away thermal energy, solve no longer along the bottom of a pan spilling
The heat energy loss phenomenon of the 20%-30% for fuel gas supply total amount of heat of having determined, while making the environment of surrounding no longer because by high temp fire
Heat that flame is taken away and improve temperature, improve the operating environment in kitchen;The stove circle 2 is hollow interlayer, the stove circle
2 internal layer double wall 21 is equipped with several return air inlets 211, the internal cavities of the stove circle 2 and the intake adit 4 close to its oral area
Connection.
Position in the stove circle 2 close to bottom end, which is equipped with, is connected to the combustion chamber 5 and external exhaust gas auxiliary exhaust mouth 22,
By outside the gas discharge combustion chamber after full combustion, the combustion gas in combustion chamber can be made preferably to mix with fresh air, sufficiently
Burning, inhibits the generation of pernicious gas.
The outer surface of the stove circle 2 is covered with thermal insulation material 8, and the inner surface of the stove circle 2 can also be covered with thermal insulating material simultaneously
Material 8.Scattering and disappearing for heat can be prevented in this way, while also making the environment of surrounding no longer because heat scatters and disappears and improves temperature.
Blower is advertised air into combustion chamber from air intake, intake adit, air outlet slit, in the combustion chamber and from confession
Port enters indoor combustion gas of burning by orifice atomization and mixes and burn, and heats to water tank, also makes the Indoor Air that burns
The temperature of body is got higher, most of insufficient high-temperature gas (at this moment the temperature of high-temperature gas can reach 800 DEG C or more) meeting of burning
By return air inlet, combustion chambers burn is returned to once again by the internal cavities, intake adit and air outlet slit of stove circle, makes burning not
The heat of sufficient high-temperature gas is not only recycled, and can make its full combustion, greatly reduces the use of combustion gas
Amount, and inhibit the generation of the carbon monoxide, hydronitrogen that do great harm to human body, while the part generated in combustion chamber is useless
Gas is discharged in the gap between water tank and stove circle, due to the gap very little between water tank and stove circle, so burned flame is not
It can be overflowed from gap, keep heat losses less, the exhaust gas generated in small part combustion chamber is arranged by exhaust gas auxiliary exhaust mouth
Out.
Preferably, as shown in Figure 1, 2, the arc-shaped structure of stove circle.
Preferably, multiple air outlet slits 112 are set from lower to upper part, from the lower to the upper, air outlet slit distribution
Density was increasing before this, at a certain position, was then gradually reduced.Top by the way that multiple air outlet slits 112 are arranged is arrived down
The variation of the distribution density of portion position, it is small by the air output of upper and lower position, so that the combustion air of top to lower part gradually increases
Add, is then gradually reduced, so that even if air bolus caused by air capacity exists at maximum position, but the sky for passing through upper and lower
The amount of gas be gradually reduced so that air bolus and and then be gradually sufficiently mixed, so that air gradually and combustion gas mixing, reaches
To sufficient mixed effect, top or lower part large quantity of air is avoided to impact combustion gas suddenly, so that air forms the presence of agglomerate,
Cause the mixing of air fuel gas bad.It can make with numerical simulation the study found that by above-mentioned setting through a large number of experiments
It obtains air fuel gas to be sufficiently mixed, combustion efficiency improves 10% or so.It should be noted that above-mentioned achievement is the applicant
It is not the common knowledge of this field by what is largely studied.
Preferably, multiple air outlet slits are set from lower to upper part, and from the lower to the upper, the density of air outlet slit distribution
Increasing amplitude constantly reduces, and starts at a certain position, and the amplitude that the density of air outlet slit distribution is gradually reduced is more next
It is bigger.It being found through a large number of experiments with numerical simulation study, this setting enables to air and combustion gas more fully to mix,
Improve efficiency of combustion.
Preferably, a certain position is the middle position in 2 short transverse of stove circle.
Preferably, multiple air outlet slits 112, from the lower to the upper, the diameter of air outlet slit are arranged from lower to upper part
It is increasing before this, at a certain position, then it is gradually reduced.By the way that the top of multiple air outlet slits 112 is arranged to lower portion
The variation for the diameter set, it is small by the air output of upper and lower position so that the combustion air of top to lower part gradually increases, then by
It is decrescence small so that even if air bolus caused by air capacity exists at maximum position, but by the amount of the air of upper and lower by
It is decrescence small so that air bolus and being then gradually sufficiently mixed, so that air gradually and combustion gas mixing, reaches sufficient
Mixed effect avoids top or lower part large quantity of air from impacting combustion gas suddenly, so that air forms the presence of agglomerate, causes air
The mixing of combustion gas is bad.Air is enabled to fire the study found that by above-mentioned setting with numerical simulation through a large number of experiments
Gas is sufficiently mixed, and combustion efficiency improves 10% or so.It should be noted that above-mentioned achievement is that the applicant passes through largely
Research obtain, be not the common knowledge of this field.
Preferably, from the lower to the upper, the increasing amplitude of air outlet slit diameter constantly reduces, at a certain position
Start, the amplitude that air outlet slit diameter is gradually reduced is increasing.Find that this sets with numerical simulation study through a large number of experiments
It sets and air and combustion gas is enabled to more fully to mix, improve efficiency of combustion.
Preferably, a certain position is the middle position in 2 short transverse of stove circle.
The vertical pipe be it is multiple, along the center radially outward direction of burner, the distribution of the vertical pipe is close
It spends smaller and smaller.Numerical simulation and it was found that, along burner center radially outward direction, single vertical pipe
Received heat is smaller and smaller, and the temperature of the vertical pipe of different location is also different, to cause local heating uneven.Because with
The burning of combustion gas, combustion gas first middle part burn, the high-temperature gas then generated is moved out from center, therefore middle part is outside
Received heat gradually becomes smaller, and because outward, then because the increase of diameter causes horizontal component area bigger, leads to unit
The heat of distribution on area is also smaller and smaller, therefore the heat being distributed in each vertical pipe is caused to reduce.It will lead to so not
It is even with position vertical pipe uneven heating, cause temperature different.Vertical pipe is arranged by the different location in burner in the present invention
Density is different, so that the integral heat pipe temperature made keeps essentially identical, to improve whole heat exchange efficiency, saves material, keeps away
Exempt from local damage caused by non-uniform temperature, extends the service life of heat pipe.
Preferably, along the center radially outward direction of burner, the distribution density of the vertical pipe is smaller and smaller
Amplitude constantly increase.As the variation of vertical pipe distribution density, the present invention has carried out a large amount of numerical simulation and experiment, from
And obtain the changing rule of above-mentioned vertical pipe distribution density.By above-mentioned changing rule, material can be saved, while can also
Enough improve 9% or so heat exchange efficiency.
Preferably, the diameter and length of each vertical pipe 103 are identical.
Preferably, the vertical pipe 103 be it is multiple, it is described perpendicular along the center radially outward direction of burner
The caliber of straight tube is smaller and smaller.The reason of concrete reason is with front vertical pipe distribution density is identical.
Preferably, along the center radially outward direction of burner, the smaller and smaller width of the caliber of the vertical pipe
Degree is continuous to be increased.The reason of concrete reason is with front vertical pipe distribution density is identical.
Preferably, the distribution density and length of all vertical pipes 103 are all identical.
Preferably, the distribution density of the orifice 7 is more next along the center radially outward direction of combustion head 3
It is smaller.Guarantee that combustion gas is gradually increased externally to intermediate distributed number, a large amount of combustion gas is located at medium position full combustion, combustion
From middle part burning, then flue gas enables the whole heating surfaces of flue gas to be heated, guarantees from the discharge of return port 211 when burning
That integrally heats is uniform.
Preferably, the distribution density of the orifice 7 is more next along the center radially outward direction of combustion head 3
Smaller amplitude is continuously increased.As the variation of orifice distribution density, the present invention has carried out a large amount of numerical simulation and experiment,
To obtain the changing rule of above-mentioned distribution density.By above-mentioned changing rule, it can be further ensured that the uniform of heating.
Preferably, the diameter of the orifice 7 is smaller and smaller along the center radially outward direction of combustion head 3.
Preferably, the diameter of the orifice 7 is smaller and smaller along the center radially outward direction of combustion head 3
Amplitude be continuously increased.Main cause with it is as before.
Preferably, as shown in Figure 1, water tank 105 and burner form ball structure, the ball 104 divide for top and
Lower part two parts, top are water tank 105, and lower part is burner.It, can be by heat pipe and the fluid of heat exchange by above-mentioned setting
It is all provided entirely in ball, exterior space can be made full use of in this way, achieve the purpose that compact-sized.
Preferably, as shown in Figure 1, the sectional area on the top is the 50-80% of lower section product, further preferably
60-70%.By above-mentioned area distributions, the heat absorption of heat pipe and heat dissipation can be made to achieve the purpose that uniformly to coordinate.
Preferably, the vertical portion 101 of the heat pipe 10 is close as shown in Figure 1, two heat pipes are arranged in the ball
Setting.
Fig. 2 illustrates the embodiment of second distribution of the heat pipe in flue.As shown in Fig. 2, 105 section of water tank
For trapezium structure.The upper bottom of trapezium structure is located at the top of vertical portion 101, and bottom is located at horizontal component top.Pass through setting
New-type trapezium structure shown in Fig. 2, can be further improved heat exchange efficiency.Because the vertical portion with heat pipe is upward, heat
The vertical portion of pipe constantly participates in exchanging heat, therefore vertical portion temperature of lower highest, by the way that trapezium structure is arranged, can make
Lower part hot water is more, and top hot water is few, achievees the purpose that uniform heat exchange.And by setting trapezium structure, external knot can be made
Structure is compact, and exterior space may be implemented to make full use of.Such as other objects can be arranged in the position of trapezium structure waist, such as need
The object to be dried.
Preferably, the upper bottom of the trapezium structure is the 40-60% of bottom, it is further preferred that 50%.
Preferably, it is described it is trapezoidal be isosceles trapezoid.
Further preferably, the trapezoidal bottom and kidney-shaped at angle be 29-67 °, preferably 40-50 °.
By above-mentioned structure optimization, uniform and heat exchange efficiency the raising of heat exchange can be realized to the full extent.
Fig. 6 illustrates the embodiment of third distribution of the heat pipe in flue.As shown in fig. 6, the water tank is rectangle
Structure.The upper bottom of rectangular configuration is located at the top of vertical portion 101.It, can be with by the way that new-type rectangular configuration shown in fig. 6 is arranged
Further such that external structure is compact, exterior space may be implemented to make full use of.Preferably, the long side of the rectangular configuration with
Vertical portion is parallel.
Preferably, the long side of rectangular configuration is 1.5-3 times of short side, preferably 2 times.
Preferably, the short side of rectangular configuration is 0.6-0.8 times of 106 radius of exhaust gases passes, preferably 0.72 times.Pass through
Above-mentioned structure optimization can realize the raising of heat exchange efficiency to the full extent.
In addition, evaporation ends of the present invention by the multiple vertical pipes 103 of setting as heat pipe, so that each vertical pipe 103 is made
The absorption of heat is added for independent absorbing pipe one by one, also increases the endotherm area of integral heat pipe evaporation ends.
Preferably, the horizontal component 102 is flat tube structure, vertical pipe 103 is circular tube structure.It is horizontal by setting
Part is flat tube structure, can increase the distribution of vertical pipe 103, further increase the absorption of heat.
Further preferably, horizontal component 102 is semi-circular structure.
Preferably, as shown in figure 4, the vertical pipe 103 surrounds the center annular Multi-layers distributing of horizontal component 102.
Preferably, axial centerline be arranged vertical pipe 103, along central axis be arranged multilayer vertical pipe 103, every layer
The axis of vertical pipe 103 is identical at a distance from central axis, to be formed using 102 central axis of horizontal component as the circular arc in the center of circle
Structure.
By numerical simulation and experiment discovery, the distance between vertical pipe 103, including at same diametrical position distance and
The distance between adjacent layer cannot be too small, too small to will lead to heat pipe distribution excessively, causes the caloric receptivity of every heat pipe insufficient, excessive
It is very little to will lead to heat pipe distribution, heat pipe is caused to overheat, therefore the application is summed up next hot by a large amount of numerical simulation and experiment
The distribution for the optimization that pipe vertical pipe 103 is distributed, the deficiency so that heat pipe can neither recept the caloric, and it is excessive to recept the caloric.
As shown in figure 8, the internal diameter of the horizontal component is D, the outer diameter of vertical pipe 103 is d, the adjacent heat of same layer
The circular arc of tube hub axis is N, and the center of circle of the circular arc is the central axis of storage heater, diameter of a circle M2 where same layer, phase
The diameter of a circle M1 of adjacent internal layer, then meet claimed below:
Sin(N)=a-b*S2- c*S, wherein Ln is logarithmic function, and S=d/ (M2-M1), a, b, c is parameter, is met as follows
It is required that:
0.795<a<0.805, 0.525<b<0.535,0.895<b<0.905;
Preferably, a=0.803, b=0.529, c=0.903.
Preferably, gradually becoming smaller with M2/D, a is increasing, b, and c is smaller and smaller.
Preferably, 0 ° < N < 120 °.
Preferably, 10 ° < N < 70 °.
Above-mentioned empirical equation is to be obtained by a large amount of numerical simulations and experiment, and pass through verification experimental verification, and error is substantially
Within 3%.
Preferably, the heat absorption capacity 900-1100W of heat pipe, further preferably 1000W;
100-120 degrees Celsius of temperature, further preferably 110 DEG C of dry rammell.
The internal diameter of horizontal component is that D is 900-1100 millimeters, further preferably 1000 millimeters.
Vertical pipe 103 is 9-10 millimeters, further preferably 9.5mm.
Certainly, Fig. 8 shows only 3 layers of heat pipe, can actually be more than three layers.M2, M1 of Fig. 8 is also only an act
Example, can actually be using the heat pipe of central axis as the layer where M1, i.e. M1=0, using current M1 as the layer where M2.
Preferably, as shown in figure 5, communicating pipe 107 is arranged between at least two adjacent vertical pipes 103.Under study for action
It was found that during vertical section heat absorption, it may appear that the absorption heat of the absorbing pipe of different location is different, leads to vertical pipe 103
Between pressure or temperature it is different, will lead to straightened portion pipe 103 in this way and be heated excessively high, cause the lost of life, once one
Vertical pipe 103 goes wrong, and may cause the problem of entire heat pipe is not available.The present invention, which passes through, largely to be studied,
Communicating pipe 107 is arranged in adjacent vertical pipe, can make in the case where vertical pipe is heated different to cause pressure different
Fluid in the big vertical pipe 103 of pressure quickly flows to the small vertical pipe 103 of pressure, to keep integral pressure balanced, keeps away
Exempt from hot-spot or supercooling.
Preferably, multiple companies are arranged between adjacent vertical pipe 103 from 103 lower part of vertical pipe to 103 top of vertical pipe
Siphunculus 107.By the way that multiple communicating pipes are arranged, fluid continuous counterpressure in heat absorption evaporation process is enabled to, is guaranteed whole
Pressure in a vertical pipe is balanced.
Preferably, constantly subtracting the distance between adjacent communicating pipe 107 from 103 lower part of vertical pipe to 103 top of vertical pipe
It is small.This purpose is in order to which more communicating pipes are arranged, because of flowing up with flue gas, heat pipe is constantly heated, with stream
Body is constantly heated, heated more and more uneven in different thermal-collecting tubes, therefore by above-mentioned setting, can guarantee in fluid stream
Reach pressure equilibrium during dynamic as soon as possible.
Preferably, constantly reducing the distance between adjacent communicating pipe from 103 lower part of vertical pipe to 103 top of vertical pipe
Amplitude it is increasing.It is found through experiments that, above-mentioned setting, can guarantee more excellent during flow of flue gas to reach pressure faster
Power is balanced.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Preferably, from 103 lower part of vertical pipe to 103 top of vertical pipe, the diameter of communicating pipe 107 is continuously increased.This mesh
Be to be arranged and guarantee bigger connection area, because of flowing up with flue gas, fluid is constantly heated, with heat pipe
It is continuous heated, it is heated more and more uneven in different thermal-collecting tubes, therefore by above-mentioned setting, it can guarantee in flow of flue gas
Reach pressure equilibrium as soon as possible in the process.
Preferably, from 103 lower part of vertical pipe to 103 top of vertical pipe, the ever-increasing amplitude of the diameter of communicating pipe 107
It is increasing.It is found through experiments that, above-mentioned setting, can guarantee that more excellent during flow of flue gas to reach pressure equal faster
Weighing apparatus.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Heat pipe horizontal component shown in Fig. 4 is preferably semicircular structure, and diameter is 400-600 millimeters, further preferably
500 millimeters.
103 outside diameter d of vertical pipe is 9-12 millimeters, further preferably 11mm.
Preferably, as shown in Figure 1, including two heat pipes, the horizontal component 102 of described two heat pipes in the system
It is respectively facing opposite direction and extends by two symmetrical heat pipes of setting, can absorb heat in different directions, meet heat exchange
Demand.
Preferably, communicating pipe is arranged between the vertical pipe 103 of adjacent heat pipe.Such as two heat pipes adjacent to each other
Communicating pipe 107 is set between vertical pipe 103., can be even to avoid uneven heating between heat pipe evaporation ends by the way that communicating pipe is arranged, it is real
Pressure between existing heat pipe is balanced, defect caused by avoiding the uneven heating between different heat pipes even.
Preferably, constantly subtracting the distance between adjacent communicating pipe 107 from 103 lower part of vertical pipe to 103 top of vertical pipe
It is small.This purpose is in order to which more communicating pipes are arranged, because of flowing up with fluid, fluid is constantly heated, with stream
Body is constantly heated, heated more and more uneven in different heat pipes, therefore by above-mentioned setting, can guarantee to flow in fluid
Reach pressure equilibrium as soon as possible in the process.
Preferably, constantly subtracting the distance between adjacent communicating pipe 107 from 103 lower part of vertical pipe to 103 top of vertical pipe
Small amplitude is increasing.It is found through experiments that, above-mentioned setting, can guarantee more excellent in process fluid flow to reach faster
Pressure is balanced.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Preferably, from 103 lower part of vertical pipe to 103 top of vertical pipe, the diameter of communicating pipe 107 is continuously increased.This mesh
Be to be arranged and guarantee bigger connection area, because of flowing up with fluid, fluid is constantly heated, with fluid
It is continuous heated, it is heated more and more uneven in different heat pipes, therefore by above-mentioned setting, it can guarantee to flow in fluid
Reach pressure equilibrium in journey as soon as possible.
Preferably, from 103 lower part of vertical pipe to 103 top of vertical pipe, the ever-increasing amplitude of the diameter of communicating pipe 107
It is increasing.It is found through experiments that, above-mentioned setting, can guarantee that more excellent in process fluid flow to reach pressure equal faster
Weighing apparatus.This is also the optimal mode of communicating got and largely studying pressure changes in distribution rule.
Although the present invention has been disclosed in the preferred embodiments as above, present invention is not limited to this.Any art technology
Personnel can make various changes or modifications, therefore protection scope of the present invention is answered without departing from the spirit and scope of the present invention
When being defined by the scope defined by the claims..
Claims (6)
1. a kind of gas steam generator, including water tank and heat pipe, the water tank includes water inlet and steam (vapor) outlet, the heat pipe
Including vertical portion, horizontal component and vertical pipe, wherein the bottom end of vertical portion is connected to horizontal component, the horizontal component lower part
Multiple vertical pipes are connected to, wherein vertical pipe is the evaporation ends of heat pipe, and vertical portion is the condensation end of heat pipe, and the vertical portion is stretched
Enter to water tank bottom, the vertical pipe and horizontal component are arranged in gas burner;It is characterized in that, the vertical pipe is
Multiple, along the center radially outward direction of burner, the distribution density of the vertical pipe is smaller and smaller;
Along the center radially outward direction of burner, the amplitude that the distribution density of the vertical pipe is smaller and smaller constantly increases
Add;
Direction of the horizontal component from the bottom end of vertical portion away from vertical portion extends, and the vertical portion is more
Extend to the pipe of water tank bottom.
2. steam generator as described in claim 1, which is characterized in that the burner includes burner seat, the burning
It is fixedly installed with the stove circle for placing water tank on device seat, the burning for being equipped with several orifices is fixedly mounted in the burner seat
Head, the bottom of the burner seat are equipped with fuel gas conduit, and the burner seat is equipped with several supply combustion head combustion adjuvants
Air outlet slit, the outside of the burner seat are equipped with the intake adit being connected to the air outlet slit, set on the intake adit
There is air intake;The stove circle, the water tank bottom and the burner seat form combustion chamber, and the stove circle is hollow folder
Layer, the internal layer double wall top of the stove circle are equipped with several return air inlets, and the internal cavities of the stove circle and the intake adit connect
It is logical.
3. steam generator as claimed in claim 2, it is characterised in that: the arc-shaped structure of stove circle.
4. steam generator as described in claim 1, which is characterized in that the horizontal component is flat tube structure, vertical pipe
For circular tube structure.
5. steam generator as claimed in claim 4, which is characterized in that horizontal component is semi-circular structure, and the vertical pipe is enclosed
Around the center annular Multi-layers distributing of horizontal component.
6. steam generator as claimed in claim 5, which is characterized in that vertical pipe is arranged in axial centerline, along center
Multilayer vertical pipe is arranged in axis, and the axis of every layer of vertical pipe is identical at a distance from central axis, to be formed in horizontal component
Mandrel line is the arc structure in the center of circle.
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CN201053838Y (en) * | 2007-05-16 | 2008-04-30 | 中山大学 | Temperature-uniform loop heat pipe device |
CN101196308A (en) * | 2007-12-20 | 2008-06-11 | 姜亦迎 | Air thermalization gas burner |
DE102009059090A1 (en) * | 2009-12-18 | 2011-06-22 | Bombardier Transportation GmbH, 10785 | Preheating an internal combustion engine |
CN202329321U (en) * | 2011-12-01 | 2012-07-11 | 中国科学院工程热物理研究所 | Gravity heat pipe with condensing section switching function |
CN103528039B (en) * | 2012-07-05 | 2015-03-25 | 朱杰 | Fuel gas heat pipe boiler |
CN203857855U (en) * | 2014-05-21 | 2014-10-01 | 乐陵市华源节能设备有限公司 | Spiral fin heat tube |
CN106052439B (en) * | 2016-07-22 | 2017-09-29 | 金陵科技学院 | A kind of runner phase change heat exchange device and method of work |
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