• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a method and a device for the generation of hot air. According to the invention hot gases are generated in a heating space (1), and water is added to these gases so that it is evaporated and mixed with the gases. In order to provide a complete mixing and good heating properties, the hot gases are passed from the heating space (1) into a whirl chamber (2) in which the gases are brought into a whirling movement. Water is fed into the whirl chamber (2) essentially adjacent the central shaft (10) of the chamber so that the water is mechanically mixed with the hot gases when it is displaced to the periphery of the chamber by the action of the whirling movement of the gases and is evaporated by means of the heat energy contained in the hot gases. The mixture of the hot gases and the evaporated water is discharged from the whirl chamber (2) essentially at a point adjacent the central shaft (10) of the chamber at the opposite side of the chamber with rspect to the water supply point.
    公开号:SU1715213A3
    申请号:SU4028908
    申请日:1987-02-03
    公开日:1992-02-23
    发明作者:Вяянянен Раймо
    申请人:Ой Партек Аб (Фирма)；
    IPC主号:
    专利说明:

    This relates to a method for producing hot air, according to which hot gases are produced in a heating space, with water and trm added to them so that it evaporates and mixes with the gases.
    Thus, the invention relates to direct-acting hot air generators, in which a mixture of gas and water vapor is supplied to the heated object through the same pipe.
    In known direct-action hot air generators, only so-called secondary air is mixed with hot flue gases, and in air circulation systems - a mixture of flue gases returning from the process, whereas in known direct-action steam generators water is mixed with hot flue gases in the furnace itself.
    A disadvantage of known hot air generators is the need for extremely large amounts of air to transfer energy in a system where air is used as the working medium. Because of this, fans, fan installations, and heat distribution piping systems must be very large. In addition, a typical feature of a known system is a relatively small pressure of air supplied by a fan, which is usually below 0.01 bar. Due to the low pressure, the heated gases cannot penetrate into the raw materials consisting of grains of small size, for example, smooth stone particles with a size of 0-8 mm. To heat raw materials containing fine particles, expensive heat-distributing devices are required that are easily clogged. In addition, when
    The use of such materials causes a difficult dust problem due to large amounts of air, as well as large energy losses due to large volumes of exhaust air,.
    In addition, a disadvantage of the prior art direct steam generator systems is the need for a large amount of water in comparison with the effect such a system provides. The reason is that water and flue gases are not completely mixed and flow through the same tube partly separately from each other. As a result, steam generators of this type are mainly used to produce hot water using heat exchangers. Known systems are suitable for direct heating of raw materials only in those processes that allow the use of large quantities of water. Another disadvantage of the known systems is that their structure does not allow high temperatures. Such systems can only be used in the combustion of gas, since the supply of water to the furnace with oil feed leads to cooling of the combustion space, which in turn leads to incomplete combustion, harmful to BO in many respects.
    The purpose of the invention is to increase efficiency.
    This goal is achieved by the fact that hot gases pass from the heating space into the vortex chamber and are given a vortex motion, water is fed into the vortex chamber practically near the central axis of the chamber so that water is mechanically mixed with the hot gases. the periphery of the chamber under the action of the vortex motion of gases and evaporates due to thermal anergy contained in these gases, a mixture of hot gases and evaporated water is released from the vortex chamber practically adjacent to the central axis camera from its opposite side relative to the point of water supply.
    In the proposed device, an exhaust pipe for hot gases (gas duct) is provided in the heating space, the exhaust pipe is connected to the periphery of the vortex chamber in order to give the hot gases a vortex motion, in the vortex chamber there are means for supplying water that opens into the chamber near its central axes as well as an exhaust pipe for a mixture of evaporated water and hot gases, said pipeline starting next to the central axis on the opposite side of the chamber
    relative to the inlet of the water supply means.
    Thus, with the help of small amounts of air, large amounts of air can be transmitted.
    heat capacity. In this case, the amount of air is 1/20 compared to known systems, for example, in a hot air generator for 500 kW, 14000 m of air is used per hour, while using the proposed system, the same 500 kW is provided at 690 m of air per 1 hour In addition, with a lower fan power, large heat capacities can be transferred, for example for transferring heat capacity 500
    5 kW before required the power of the fan installation of 90 kW, and using the proposed system requires only 15 kW. Thus, the saving on fan power is 75 kW. Thanks
    With less air, heat distribution pipes can be used much smaller than in known systems, for example, with a power of 500 kW, a fan pipe with a diameter of 500 mm is required, and when using the proposed system, the required diameter is only 100 mm.
    Since the proposed device uses a mixture of hot gases and water,
    0 The condensation of water mixed with a gas provides a more complete transfer of energy to the heating material (in our example, this material is sand). There is no problem with the invention.
    5 dust, because the hot gases are humid and, in addition, the amount of air is small. In the proposed technical solution, higher pressures can be used than in known systems. In our example, energy can be supplied to a material with a small particle size without the use of expensive and cumbersome means of air distribution, and the pressure can be increased five times compared with the known system, namely, pressures equal to 0.1 and 0.5 bar. In our example, in the device according to the invention, water was supplied to the vortex chamber at 500 kW at a speed of about 5 liters / min. Accordingly, with equal
    0, the amount of water required for a known steam generator is about 13 liters per minute. The resulting difference is a consequence of the fact that in the proposed device the temperature of the mixture is higher and in the vortex chamber of the generator full mixing and overheating of water with hot flue gases can occur. The hot air generator of the invention cannot be called a steam boiler for a steam generator, since water evaporates
    not in a water jacket, not in a system of water pipes or in a firebox, but in a vortex chamber with the combined action of centrifugal and thermal energy. Due to this feature, the generator can work with energy of any kind, if only hot gases are supplied to the vortex chamber. It is also possible to use direct electric heating or a battery for heating air. The vortex chamber system of the present invention makes it possible to use completely dry blast furnaces, for example, mass or brick kilns with oil, gas, peat, etc. feed. Possible use and power. Battery power means that heat energy is accumulated, for example, in stone material, from where it is transferred by air as a working medium into the vortex chamber.
    In the proposed system, to achieve the required fan temperature, automatic adjustment is used, the temperature ensuring the supply of the required amount of water. Due to this, it is possible to simply supply hot air without any cooling of water or water jacket, which is used in known steam generation systems when the accumulated energy is exhausted. Another advantage of dry food stoves is to eliminate the danger of freezing, provided that the water supply pipe does not freeze. Another advantage of the device proposed is that there are no high pressure tanks in it, since the water space is open or not provided at all. The control of the combustion of petroleum or gas in the hot air generator of the present invention can be carried out both manually and automatically. The control can be carried out by passing compressed flue gases through clear water, whereby it is possible to judge from the darkening of the water whether the flame burns correctly or not. The control vessel may be located within the field of view of the user so as to continuously or periodically control the combustion. Note that a slight excess of air is not a disadvantage, since the heating is carried out with real flue gases. Therefore, the control is intended mainly to monitor the purity of the combustion, and this is extremely easy to do with water analysis, since the smallest amount of oil will look like a film on the surface of the water, very noticeable in water and soot. Soot appearance
    Combustion of gas is caused by insufficient air supply, as will be seen from the water analysis. The advantage of the proposed technical solution is that it is very easy to provide a safety valve in the system. A branch for the safety valve can be removed from the discharge pipe. In this case, the safety valve is adjusted to the limiting point when the amount of air from the burner fan drops to a minimum and the combustion takes place with a lack of air. The safety valve can be adjusted below the opening point of the safety valve of the piston compressor, then partial opening of the safety valve, but the compressor valve does not reduce the air supply. In addition, a thermostat is provided that acts as a leak detector for the pressure relief valve on the charge side, if the temperature in the pipeline of the pressure relief valve becomes too high, the thermostat is released. With instantaneous pressure jumps, the thermostat release does not occur, thereby preventing unwanted interruptions in operation. Such a design of the safety valve provides an excessively flexible use of the device in comparison with the known systems.
    FIG. 1 shows the proposed device: a general view from the side; in fig. 2 - the same, in a different projection.
    In the device {FIG. 1) The heating space 1 is an oven. The vortex chamber 2 communicates with the furnace through the exhaust gas duct 3. Inside the furnace wall, an open water space 4 is formed that surrounds this furnace. A so-called flame tube 5 is also provided in the furnace, preventing heat transfer by radiation from the flame in the furnace to the water. The water space 4 communicates with the vortex chamber 2 by means of the pipe connection 6, while the gases are withdrawn from the vortex chamber through the discharge channel pipeline 7.
    An essential feature of the invention is that the furnace does not serve to evaporate the water contained in the water space 4, as in the known steam generators. The temperature of the water in the water space 4 is always below 100 ° C, i.e. below the water vaporization point. Excessive heating of the water enclosed in the water space 4 is prevented by the flame tube 5, which prevents the transfer of heat of radiation from the flame to cold water. Zharov pipe 5 is installed on such
    distance from the water space 4, which does not exceed the maximum temperature permissible for the material of the flame tube, i.e. the water enclosed in the water space A acts as a cooler for the flame tube 5. It is particularly preferable to apply the flame tube 5 with oil feed, since the flame tube raises the temperature in the combustion space to a temperature exceeding 1000 ° C, to the welfare of complete oil burning . Due to the use of the flame tube 5, conditions are achieved that correspond to the conditions in the ceramic combustion chamber. The flame tube 5 is made of a thin material, since within a few seconds after the flame ignites, the temperature in the combustion space rises to its maximum value.
    The water space 4 arranged inside the furnace wall communicates with the vortex chamber 2 through a large diameter bypass pipe 8. This results in an open structure, whereby the water space does not under any circumstances turn out to be closed and the pressure in the water space never exceeds the maximum pressure in the air ventilator.
    Another essential feature of the invention lies in the use of a vortex chamber 2 for mixing hot gases and water. Hot gases come from the furnace through a relatively narrow exhaust pipe 3 to the vortex chamber. The end of the discharge conduit 3 is located on the periphery of the vortex chamber, as a result of which a vortex motion is attached to the gases. Under the action of centrifugal force, hot gases are pressed against the periphery of the vortex chamber. Water is supplied to the vortex chamber 2 through the pipe and the valve 9 at the lower region of the water space; water enters the center of the vortex chamber, i.e. near the central axis of chamber 10, with periodic or continuous adjustment of valve 9 for dosing. As soon as water enters the vortex chamber, it is carried to the periphery, where it acquires a vortex motion along with hot gases. Since the water is jelly of hot gases, it cannot escape from the vortex chamber until it has completely evaporated and combined with hot gases. The mixture of steam and gas in the vortex chamber can be overheated to a higher temperature, however, the amount of water is very small compared with the heat output. This moment is very important, because of the condensation of water in the heating process, problems arise with the heated material or with the environment. In principle, the temperature of the mixture can be continuously controlled in the range of 80–400 ° C. At lower temperatures, the device acts as a hot water generator or as a steam generator.
    Adjusting the amount of water you can
    0 to produce as a function of the temperature of the mixture using a water valve or a metering device operating continuously or over time intervals. If the metering device is a magnetic valve
    5 or a similar device, the valve 9 supplying water to the vortex chamber and the valve 11 supplying water to the water space 4 are opened simultaneously. The adjustment of said water flows is carried out so that they match each other, i.e. so that the amount of water taken from the water space 4 is equal to the amount of water added to the same space. If the amount of water supplied to the vortex chamber is less than the amount of water supplied to the water space 4, the water flows into the vortex chamber 2 through the overflow pipe 8, as a result of which an equilibrium state is automatically reached. The overflow pipe 8 is connected to the vortex chamber at the same point as the pipe 6. The advantage of this design is that you can continuously replenish the water in the water space 4, while the water surface 8 water space is always on the right level If there is an excessive lowering of the surface of the water enclosed in the water space
    0 4, the surface electrode opens the valve 11 and the surface of the water rises to the desired level. The filling of the water space 4 always occurs on command from the electrode 12, when it detects the absence of water, regardless of the operation of the burner or the need of the temperature controller in water.
    If, when the device is turned off, the condensed water flows into the vortex
    0 chamber 2 and discharge pipe 3, then the next time the device is turned on, water is removed in the same way as water supplied to the vortex chamber. Accordingly, an automatic return system is provided for the condensed water.
    The considered water control system also provides extremely accurate temperature control of the bleed. In the case of the use of a proportional integral-differential controller, it is possible to achieve an adjustment accuracy of 1%, i.e. extremely accurate water quality control will occur.
    From the vortex chamber, the mixture is discharged through the exhaust pipe 7, the exhaust pipe 7 is connected to the vortex chamber 2 near its central axis 10 on the opposite side of the pipe b and the overflow pipe 8. This arrangement is clearly seen in FIG. 2. Through pipe 7, the mixture can be supplied to the site of application. In this case, the place of use is the sand pad 13.
    . An advantage of the method and device of the present invention is the possibility of very precise control of all quantities of water. In addition, in the vortex chamber, almost complete mixing of water with hot gases occurs. As a result, the required amount of water is small compared to the capacity. Due to the listed properties, the mixture is equivalent to superheated steam at very high pressure, even if the device is used as a hot air generator and the vapor pressure is below 1 bar and mostly below 0.5 bar.
    If the back pressure created in the process is large and prone to change, then a rotary piston compressor is used as a fan in which the amount of air varies very slightly with the back pressure. A rotary piston compressor is used in a pressure range of about 1 bar. If the back pressure is lower than 0.5 bar, high pressure fans can be used as a blower, and the amount of air in them is strongly dependent on the back pressure. In the case of fans, it is required that back pressure variations are accurately known and these variations occur only within a narrow range.
    The device works as follows.
    Combustion air passes through a filter and a sound absorber 14 into a rotary piston compressor 15. A pressure switch 16 serves to achieve the required air pressure for combustion, the valve is removed to start the burner, and the initial stage starts. The automatics of the burner turn on the transformer 17 in order to facilitate the ignition process. The oil pump 18 is turned on, and after some time the magnetic valve 19 opens for oil. As soon as the pressure is about 20
    The oil bar comes out of the burner 20 outlet. It ignites with a high voltage spark from the transformer. A photoresistor 21 serves to detect a flame. Oil pressure is regulated by regulator 22.
    After ignition in the furnace inside the flame tube 8, the flame starts to burn. An air gap of approximately 10 mm is provided between the fat tube 5 and the body of water. The temperature in the furnace is very high, but thanks to this design, the water in the water space 4 does not perceive the heat of radiation and heat transfer is due to thermal conductivity, and the water temperature cannot rise to evaporation temperature, it is always below 100 ° C during normal operation. The water in the water space 4 begins to circulate with the opening of the valve 9 placed in the pipe connection 6 between the vortex chamber 2 and the water space, the valve 11 also opens at the same time. As a result, cold water continuously flows into the water space 4 and the surface of the water is kept at a constant level. If the water flow through the valve 11 exceeds the water flow entering through the valve 9 into the vortex chamber, then an excess water flow enters the vortex chamber 2 via the overflow pipe 8. Valves 9 and 11 are controlled from a proportional integral-differential temperature controller 23 in response to the measurement results from a temperature sensor. If the level of the surface of the water enclosed in the water space 4 is below the electrode 12, only the valve 11 opens;
    The combustion air supply to the burner is carried out on the primary-secondary principle in such a way that the amount of air is controlled by a hinged valve 24, which is manually controlled. If valve 24 is throttled, the flow of primary air increases, when the valve opens, the flow of secondary air increases. The hot gases produced during combustion flow through the exhaust pipe 3 into the vortex chamber 2. In the vortex chamber, the hot gases acquire a rotational motion, and water, also fed into the vortex chamber, flows to the vortex motion from the center of the chamber to its periphery. and remains there until evaporation due to the combined action of centrifugal energy and heat. The mixture of water and gas is discharged from the vortex chamber through the exhaust pipe 7,
    The continuous measurement of the temperature of the mixture is carried out by the temperature control unit 23 of the temperature regulator located on the outlet pipe 7, and if necessary, water is added in accordance with the foregoing. The pressure switch 25 shuts off the burner when the switch setting is exceeded for a certain length of time. The pressure information can be sent to the control unit using a pressure sensor 26. In turn, the thermostat 27 for protection against excessive heat is released when its setpoint is exceeded. If during the process the backpressure exceeds the set point of the safety valve 28, then the blower channel opens, connected to the atmosphere, while the thermostat 29 turns off the burner with a certain time delay. The overpressure thermostat 29 also disengages in the event of a leak in the safety valve 28, then the thermostat acts as a so-called leak detector.
    In the considered embodiment, the gas mixture from the vortex chamber 2 enters the heated material, for example, sand pad 13, and penetrates there, and the water contained in the mixture condenses in the sand pad, releasing thermal energy. At the same time, the formation of moisture prevents the occurrence of dust and the drying of the sand pad. In the sand bed, the water obtained during the combustion process also condenses, so that the burning efficiency can be equal to 100% or more per set specific heat capacity of the oil.
    Naturally, this requires that the flue gases are cooled below the dew point of the flue gases. This type of cooling is provided when mixed with ice cream sand.
    The burning control can be maintained automatically with the help of a transparent reservoir 30. In this case, the hot gases automatically pass through the water enclosed in the reservoir at intervals specified by the valve 31 so. so that incomplete combustion can be immediately detected by changing the color of pure water. The number of tanks is selected as needed.
    For measuring the amount of water supplied to the water space 4, as well as the pressure, the corresponding means 32 and 33 are used. The temperature in the water space 4
    limiter 34 is controlled. Limiter 34 is adjusted to 93 ° C, and when this temperature is exceeded, the limiter turns off the burner.
    A variety of modifications of the invention are possible. The heating space 1 does not need to be a furnace or a firebox, it is possible to use it in other structures, for example, electric heating. Heating space 1 also
    can be replaced by some other process whereby the hot gases are released into the vortex chamber. The water supply to the vortex chamber can also be arranged from a suitable container, etc.
    权利要求:
    Claims (2)
    [1]
    1. A method of producing hot air by generating hot gases in the heating space, tangentially feeding them into the vortex chamber to produce a swirling flow with their subsequent discharge through the central zone of the latter, entering water into the hot gases to heat it in
    the mixing process, characterized in that, in order to increase efficiency, water is introduced into the central part of the swirling flow, the heating during the mixing process is carried out in a swirling gas flow until it is fully evaporated and the removal is carried out in the form of a mixture of the produced steam with the gas.
    [2]
    2. A device for producing hot air, containing a heating space for producing hot gases, connected tangentially with a flue gas duct to the periphery of the vortex chamber, provided with an opening for removing a mixture of steam and gas along the axis of one of the ends and connected to a device for adding water to the hot gases, which are due to the fact that, in order to increase the efficiency, the vortex is connected to the device for adding water to the hot gases along the axis
    its other end against the hole for removal of the mixture of steam and gas.
    /
    1
    25 26
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    同族专利:
    公开号 | 公开日
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    DK161478C|1991-12-16|
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    引用文献:
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    US2223597A|1937-12-30|1940-12-03|Jack A Brewster|Apparatus for protecting vegetation|
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    US3151850A|1962-10-04|1964-10-06|Jr Walker L Wellford|Kiln furnace|
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    US3665681A|1970-10-13|1972-05-30|Andrew H Vitenko|Smoke cleaning apparatus|
    US3656441A|1970-10-26|1972-04-18|Morse Boulger Inc|Incinerator|
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    DK148455C|1983-04-11|1985-11-25|Henrik Gerner Olrik|PROCEDURE IN OPERATION OF A LINING PLANT AND LINING PLANT TO EXERCISE THE PROCEDURE|
    US4493270A|1983-11-10|1985-01-15|Gamroth Arthur P|Heating unit|
    US4557203A|1984-08-13|1985-12-10|Pollution Control Products Co.|Method of controlling a reclamation furnace|
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    RU2552439C2|2013-07-17|2015-06-10|Общество с ограниченной ответственностью Завод "Ферингер и К"|Steam generation method and device|
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    法律状态:
    2005-05-10| REG| Reference to a code of a succession state|Ref country code: RU Ref legal event code: MM4A Effective date: 20030604 |
    优先权:
    申请号 | 申请日 | 专利标题
    FI852233A|FI72592C|1985-06-04|1985-06-04|FOERFARANDE OCH ANORDNING FOER GENERERING AV HET GAS.|
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