CN108662570B - A kind of gas steam generator of air outlet slit variable density - Google Patents

Abstract

The present invention provides a kind of gas steam generators of air outlet slit variable density, including water tank and burner, burner includes burner seat, the burner seat is equipped with the air outlet slit of several supply combustion head combustion adjuvants, the outside of the burner seat is equipped with the intake adit being connected to the air outlet slit, from lower to upper part, multiple air outlet slits are set, from lower to upper part, multiple air outlet slits are set, from the lower to the upper, the density of air outlet slit distribution was increasing before this, at a certain position, then it is gradually reduced.The present invention is by being arranged the variation of distribution density of the top of multiple air outlet slits to lower position, so that air gradually and combustion gas mixing, reaches sufficient mixed effect.

Description

A kind of gas steam generator of air outlet slit variable density

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, the air of burner and combustion gas, which exist, mixes non-uniform phenomenon, causes to burn insufficient.Therefore It is necessary to improve the mixing of combustion gas and air, make its combustion even.

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 of air outlet slit variable density, including water tank and burner, the water tank setting exist On burner, burner includes burner seat, and the stove circle for placing water tank, the combustion are fixedly installed on the burner seat The combustion head for being equipped with several orifices is fixedly mounted in burner seat, the bottom of the burner seat is equipped with fuel gas conduit, the burning Device seat is equipped with the air outlet slit of several supply combustion head combustion adjuvants, and the outside of the burner seat is equipped with and the air The intake adit of outlet, the intake adit are equipped with air intake；The stove circle, the water tank bottom and the burning Device seat forms 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, institute The internal cavities for stating stove circle are connected to the intake adit, which is characterized in that from lower to upper part, multiple air outlet slits are set, from The density of lower part to top, air outlet slit distribution was increasing before this, at a certain position, was then gradually reduced.

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.

Preferably, further including heat pipe, the water tank includes water inlet and steam (vapor) outlet, and the heat pipe includes vertical portion Point, horizontal component and vertical pipe, wherein the bottom end of vertical portion is connected to horizontal component, and the horizontal component lower part connection is multiple perpendicular Straight tube, wherein vertical pipe is the evaporation ends of heat pipe, and vertical portion is the condensation end of heat pipe, and the vertical portion extend into water tank bottom Portion, the vertical pipe and horizontal component are arranged in gas burner；The heat pipe be at least two, adjacent heat pipe it is vertical Communicating pipe is set between part.

Preferably, being continuously increased the distance between adjacent communicating pipe from vertical portion lower part to vertical portion top.

Preferably, the distance between adjacent communicating pipe is ever-increasing from vertical portion lower part to vertical portion top Amplitude is increasing.

Preferably, the vertical portion is plank frame.

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 arc-shaped structure of stove 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.

Preferably, 0.3 < d/L < 0.5.

Preferably, gradually becoming smaller with d/L, a is increasing, and b is smaller and smaller, and c is increasing.

Compared with prior art, the present invention has the advantage that:

1) variation of distribution density of the present invention by the top of the multiple air outlet slits of setting to lower position, by upper and lower The air output of position is small, so that the combustion air of top to lower part gradually increases, is then gradually reduced, so that even if maximum position Locate air capacity caused by air bolus exist, but be gradually reduced by the amount of the air of upper and lower so that air bolus and and then by Being sufficiently mixed gradually, so that air gradually and combustion gas mixing, reaches sufficient mixed effect, avoids top or lower part Large quantity of air impacts combustion gas suddenly, so that air forms the presence of agglomerate, causes the mixing of air fuel gas bad, so that air capacity In medium position maximum, the mixing of big air bolus and combustion gas is gradually diluted by the reduction of the air capacity of top and the bottom.By big The experiment of amount and numerical simulation the study found that by above-mentioned setting, enable to air fuel gas to be sufficiently mixed, combustion efficiency mentions It is high by 10% or so.

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 intake, 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, The air duct 4 is equipped with air intake 121, and the shell of the air supply line 4 coats the burner seat 1, available in this way The air that the heating of burner seat 1 enters, 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 make Water tank is heated evenly, the temperature in fast lifting pot, and the stove circle 2, the water tank and the burner seat 1 formation prevent fire 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% of fuel gas supply total amount of heat, while making the environment of surrounding no longer because by thermal-flame The heat 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 be 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 211, combustion chambers burn is returned to once again by the internal cavities, intake adit and air outlet slit of stove circle, makes to burn The heat of insufficient 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 (7)

1. a kind of gas steam generator of air outlet slit variable density, including water tank and burner, the water tank setting is being fired In burner, burner includes burner seat, and the stove circle for placing water tank, the burning are fixedly installed on the burner seat The combustion head for being equipped with several orifices is fixedly mounted in device seat, the bottom of the burner seat is equipped with fuel gas conduit, the burner Seat is equipped with the air outlet slit of several supply combustion head combustion adjuvants, and the outside of the burner seat is equipped with to go out with the air The intake adit of mouth connection, the intake adit are equipped with air intake；The stove circle, the water tank bottom and the burner Seat forms 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, described The internal cavities of stove circle are connected to the intake adit, which is characterized in that multiple air outlet slits are arranged from lower to upper part, under The density in portion to top, air outlet slit distribution was increasing before this, at a certain position, was then gradually reduced；

From lower to upper part, multiple air outlet slits are set, from the lower to the upper, the increasing width of the density of air outlet slit distribution Degree constantly reduces, and starts at a certain position, and the amplitude that the density of air outlet slit distribution is gradually reduced is increasing；

The a certain position is the middle position in stove circle short transverse.

2. steam generator as described in claim 1, which is characterized in that further include heat pipe, the water tank include water inlet and Steam (vapor) outlet, the heat pipe include vertical portion, horizontal component and vertical pipe, and wherein the bottom end of vertical portion is connected to horizontal part Point, the horizontal component lower part is connected to multiple vertical pipes, and wherein vertical pipe is the evaporation ends of heat pipe, and vertical portion is the cold of heat pipe Solidifying end, the vertical portion extend into water tank bottom, and the vertical pipe and horizontal component are arranged in gas burner；The heat Pipe is at least two, and communicating pipe is arranged between the vertical portion of adjacent heat pipe.

3. steam generator as claimed in claim 2, which is characterized in that from vertical portion lower part to vertical portion top, phase The distance between adjacent communicating pipe is continuously increased.

4. steam generator as claimed in claim 3, which is characterized in that from vertical portion lower part to vertical portion top, phase The distance between adjacent communicating pipe, ever-increasing amplitude was increasing.

5. steam generator as claimed in claim 2, which is characterized in that the vertical portion is plank frame.

6. steam generator as claimed in claim 5, which is characterized in that the horizontal component from the bottom end of vertical portion towards Direction far from vertical portion extends, and the vertical portion is the more pipes for extending to water tank bottom.

7. steam generator as described in claim 1, which is characterized in that the arc-shaped structure of stove circle.