EP0071626A1 - Verfahren zur Vorbereitung der Reinigung der Brennschale sowie Vorrichtung zur Verbrennung von rückstandsreichen Altölen in einer Brennschale. - Google Patents
Verfahren zur Vorbereitung der Reinigung der Brennschale sowie Vorrichtung zur Verbrennung von rückstandsreichen Altölen in einer Brennschale.Info
- Publication number
- EP0071626A1 EP0071626A1 EP82900545A EP82900545A EP0071626A1 EP 0071626 A1 EP0071626 A1 EP 0071626A1 EP 82900545 A EP82900545 A EP 82900545A EP 82900545 A EP82900545 A EP 82900545A EP 0071626 A1 EP0071626 A1 EP 0071626A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- brazier
- oil
- combustion
- ignition
- trough
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000002699 waste material Substances 0.000 title claims description 42
- 238000000034 method Methods 0.000 title claims description 24
- 238000004140 cleaning Methods 0.000 title claims description 14
- 238000010304 firing Methods 0.000 title 1
- 238000002485 combustion reaction Methods 0.000 claims abstract description 55
- 239000010913 used oil Substances 0.000 claims abstract description 15
- 238000001704 evaporation Methods 0.000 claims abstract description 9
- 230000008020 evaporation Effects 0.000 claims abstract description 9
- 239000002893 slag Substances 0.000 claims abstract description 9
- 239000003921 oil Substances 0.000 claims description 88
- 238000010438 heat treatment Methods 0.000 claims description 26
- 239000000446 fuel Substances 0.000 claims description 13
- 239000010849 combustible waste Substances 0.000 claims description 8
- 239000010426 asphalt Substances 0.000 claims description 6
- 238000000197 pyrolysis Methods 0.000 claims description 5
- 230000005855 radiation Effects 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 4
- 229910001018 Cast iron Inorganic materials 0.000 claims description 3
- 238000012544 monitoring process Methods 0.000 claims description 3
- 239000000567 combustion gas Substances 0.000 claims description 2
- 238000004891 communication Methods 0.000 claims description 2
- 238000005520 cutting process Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims 1
- 238000007790 scraping Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000000779 smoke Substances 0.000 description 3
- 239000002956 ash Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 230000001965 increasing effect Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 235000012773 waffles Nutrition 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910001208 Crucible steel Inorganic materials 0.000 description 1
- 244000027321 Lychnis chalcedonica Species 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000004200 deflagration Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 230000009969 flowable effect Effects 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000012208 gear oil Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 230000002757 inflammatory effect Effects 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000002641 tar oil Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D5/00—Burners in which liquid fuel evaporates in the combustion space, with or without chemical conversion of evaporated fuel
- F23D5/02—Burners in which liquid fuel evaporates in the combustion space, with or without chemical conversion of evaporated fuel the liquid forming a pool, e.g. bowl-type evaporators, dish-type evaporators
- F23D5/04—Pot-type evaporators, i.e. using a partially-enclosed combustion space
- F23D5/045—Pot-type evaporators, i.e. using a partially-enclosed combustion space with forced draft
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D5/00—Burners in which liquid fuel evaporates in the combustion space, with or without chemical conversion of evaporated fuel
- F23D5/12—Details
- F23D5/18—Preheating devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23Q—IGNITION; EXTINGUISHING-DEVICES
- F23Q7/00—Incandescent ignition; Igniters using electrically-produced heat, e.g. lighters for cigarettes; Electrically-heated glowing plugs
- F23Q7/06—Incandescent ignition; Igniters using electrically-produced heat, e.g. lighters for cigarettes; Electrically-heated glowing plugs structurally associated with fluid-fuel burners
- F23Q7/08—Incandescent ignition; Igniters using electrically-produced heat, e.g. lighters for cigarettes; Electrically-heated glowing plugs structurally associated with fluid-fuel burners for evaporating and igniting liquid fuel, e.g. in hurricane lanterns
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
- F24C5/00—Stoves or ranges for liquid fuels
- F24C5/02—Stoves or ranges for liquid fuels with evaporation burners, e.g. dish type
Definitions
- the invention relates to a method for igniting or burning combustible, residue-rich waste oils in a furnace, the base with a brazier and above the brazier with a - optionally subdivided - combustion chamber, and with a device with which the waste oil of the brazier is metered can be supplied.
- the invention further relates to a method for preparing the cleaning of the brazier required for burning waste oil after the fuel supply has been interrupted and the combustible waste oil portion still present in the brazier has been burned out.
- the invention relates to a device for burning combustible waste oils in a brazier.
- Waste oils are understood to mean, in particular, collected oil mixtures which are produced in the service station operation. The regeneration of these waste oils is possible in principle, but it requires energy and power, which is often not justified. In many cases, these waste oils are burned. They often contain a high proportion of dirt, for example highly viscous gear oil residues, grease, carbon particles, metal abrasion and the like. These "used oils” can also contain paint residues, wood pulp parts and water. Furthermore, waste oils of the type mentioned at the outset can also be understood to include those which contain coal dust, tar oils, bilge oils, refinery waste, chemical, combustible waste and coal-water-oil mixtures.
- the quality of the waste oil can be between 0 and 10,000 kcal. 0 is practically pure water. A mixture of all components is therefore required in a storage tank in order to obtain a combustible waste oil consistency.
- So-called "old oil stoves” are known, for example from CH-PS 368 255.
- the known combustion device has a columnar housing, at the base of which a brazier is arranged.
- the fuel is metered into the brazier via a feed line.
- the feed line ends above the brazier, so that the waste oil drops from its mouth into the brazier.
- the device is ignited by first introducing egg-boiling fuel oil into the brazier and this with
- the additional heat source is switched off; the combustion of the fuel that is fed in maintains itself.
- the brazier to be heated can also be used to prepare the cleaning required for waste oil combustion. For this purpose, after the fuel supply has been interrupted and the fuel still in the brazier has been burned out, the remaining fuel (the "bitumen slag") is pyrolyzed with the aid of the heat source which is switched on again.
- the method for ignition and the device suitable for this, as well as the usual burner operation, can of course also be carried out with high-purity fuels, for example with heating oil EL, in which hardly any ash quantities are produced.
- heating oil EL heating oil
- the known stoves operated with heating oil can in no case be operated with waste oil. Therefore, the technical effort for the device described below is primarily justified for the combustion of heavily contaminated waste oils.
- the temperature of the brazier must reach both the ignition and the pyrolysis temperature, it must be possible to bring the brazier to a temperature higher than 400 ° C.
- the pyrolysis is carried out, for example, at a temperature of 700 to 800.degree. C., whereas an ignition and evaporation temperature of approx. 350 to 400.degree. Different temperatures can also be set by an appropriate thermostat control device, the brazier temperature T being between 400 ° and 800 ° C.
- a device for performing the methods and for burning combustible waste oils in a brazier has a brazier at its base. Above the brazier is a - if necessary divided - Combustion chamber arranged. It is known to let the fuel drip into the bowl from above, or to let it flow in laterally or centrally with respect to the surface of the brazier. Basically, various known inflow options can be used.
- at least one additional heating device is preferably arranged below the brazier. These additional heating devices are preferably electrically operated
- Heating coils or coils Inductive heating of the brazier is also possible.
- a switchable gas burner with a burning lance ending below the brazier. It is essential that the principle of the additional heating which can be switched on and off is observed.
- the brazier is equipped with a recess with a surface structure underneath the end of the waste oil supply line.
- This trough which has, for example, a corrugation or a waffle structure, has a somewhat thinner base and is locally provided with an increased heating, so that it heats up in a shorter time than the rest of the brazier.
- the trough has an oval or kidney-shaped outline and takes up about a fifth to a third of the bottom surface of the brazier.
- the brazier preferably has a relatively high heat capacity, it is therefore cast in particular from cast iron (DIN 1493) and then face-turned on its underside. On its upper side (flame side), the brazier is provided with concentric grooves, waffles or humps or some other surface-enlarging structure, similar to the trough area. This structure means that the suffering frost see phenomenon does not develop; on the contrary, such a surface structure means that good warm contact is quickly established between the old oil droplets and the surface.
- the size and diameter of the brazier depend on the capacity of the combustion device.
- the oil supply line preferably ends at a distance of between 2 and 20 cm, preferably between 7 and 10 cm, above the brazier or trough.
- the inflow nozzle which forms the end part of the feed line, is arranged at an angle of inclination between 25 and 35 with the horizontal.
- the inflow nozzle also has a much larger clear cross-sectional area than the actual oil supply line, which ends at the inflow nozzle. This prevents the used oil in the end region of the oil supply line from filling the entire cross-section, which generally leads to undesirable afterflow phenomena when the oil flow is switched off.
- Figure 1 shows a device for the combustion of waste oils according to the invention, seen from the side;
- Figure 2 shows the device of Figure 1 seen from the front
- FIG. 3 shows a detailed illustration with another ignition device
- Figure 4 is a plan view of part of the brazier with the trough
- FIGS. 5 and 6 an oil supply nozzle with cleaning device, seen from the side and from the front;
- Figure 7 shows a special type of fresh air supply.
- the device for the combustion of waste oil has the outer shape of a so-called warm air heater.
- a storage container 1 is arranged, in the. the waste oil is filled.
- the storage container 1 has, for example, a capacity of 145 liters.
- a sump vessel 5 projecting downwards is attached to the side of the storage container 1, in which coarse deposits separate out.
- a cylindrical strainer 6 is placed around the sump vessel 5, which shields the entrance area of a metering oil pump.
- the oil pump 2 is usually a Zahnradpur ⁇ pe or another pump that can deliver and deliver the used oil in a metering manner.
- the suction opening of the oil pump 2 is within the strainer 6 but above the sump level.
- the oil pump 2 is driven via a shaft 4 by a motor 3 which is arranged on a cover 9 above the storage container.
- a connecting to the oil pump 2 supply line 7 is from the The strainer basket 6 is led upwards and directs the pumped oil to an inflow nozzle 8.
- the oil pump 2 with its motor can be removed from the strainer basket 6 to enable cleaning after removing the cover 9.
- the inflow capacity in the illustrated embodiment is approximately between 0.5 to 3 kg of oil per hour. The pumped amount of used oil can be infinitely metered within this range.
- the actual device according to the invention in the present case designed as a hot air-generating thermal bath 10, is externally similar in size to similar devices of the same purpose.
- the device has a housing 11 which is delimited on its base side 12 by the storage container 1.
- a heat exchanger 13 is attached to the head part of the housing 11.
- An exhaust pipe 14 leads into the atmosphere via a chimney. It is possible and appropriate to also install corresponding known filters in this chimney.
- a burner box 14 is inserted, the rear wall of which forms part of the housing 11. This part of the housing is mounted on the storage container via intermediate feet 15.
- a burner pot 18 is provided within the burner box 14 and has a cylindrical wall which is at a distance which corresponds to approximately half the diameter of the burner pot. Distance from the wall of the burner box 14 has.
- a heating and insulating plate 19 In the bottom of the burner pot 18 is a heating and insulating plate 19, on which a brazier 21 is placed.
- the brazier 21 has an approximately pan or plate shape. Your upright Standing walls open from the bottom 22 of the brazier 21, so that the bowl has a larger clear width at its upper edge than corresponds to the floor area.
- the brazier 21 consists of cast iron, the wall thickness being dimensioned according to professional experience and heat capacity so that there is a constant evaporation and combustion of the incoming liquid waste oil.
- an electrical resistance wire coil 23 In the heating and insulating plate 19, directly below the bottom of the brazier 21, an electrical resistance wire coil 23 is installed, the lead wires of which, taking into account the appropriate "heat protection conditions, lead to the outside.
- the brazier 21 can reach a temperature of 350 to 800 ° C. (red heat)
- the brazier is provided with an additional heating device, namely a further high-temperature coil 28, in the area directly below the mouth of the inflow nozzle 8 28 lies directly under a recessed bottom 27 in the bottom 22 of the brazier 21, which in the present case has an approximately kidney-shaped shape and occupies approximately 15% of the bottom surface of the brazier 21.
- the bottom recess 27 is provided with a corrugated structure the waste oil droplets that have fallen into the hollow 27 be smashed directly and find the most irregular, large-area contact with the heated surface.
- a temperature sensor 37 is also installed below the brazier 21, which can also be connected directly to the brazier 21. This temperature sensor is used to monitor and control the processes as described below.
- the brazier 21 is surrounded by the burner pot 18.
- the jacket of the burner pot 18 is provided with numerous air bores 20 through which the combustion air enters.
- a support shoulder 38 is stamped into the jacket, on which a glow hood 40 rests at the edge.
- This cast steel hood 40 which can be heated to red heat, is also provided with perforations 41, so that the combustion gases, including those which have not yet been completely burned, can pass through the perforations 41 and burn in the area of the hood 40.
- the hood 40 has approximately the shape of a truncated cone, which has a further opening 42 at its upper end, into which a glow converter insert 43 can be inserted.
- the glow converter insert consists of thin wire coils, made of refractory wire. This glows after a short burning time, so that good afterburning is also guaranteed in its area. These parts ensure that all combustible components of the waste oil also burn, completely to form H 2 O and CO 2 .
- the hot, partially still burning and burned gases are passed through a combustion chamber 30 through the lateral surfaces of the glow hood 40, which form an angle of approximately 30 to 60 ° with respect to the horizontal, which directly adjoins the burner box 14 upwards connects.
- the combustion chamber 30 is also cylindrical.
- the jacket 31 of the combustion chamber 30 is wing-like provided with numerous radiation fins 32 which improve the thermal contact with the air flowing past on the outside.
- the combustion chamber 3 ⁇ is closed at the top by a cover 33 and opens into an outlet opening 34, which is directly followed by the labyrinth heat exchanger 13.
- the inlet port 8 is shown.
- the mouth 50 of the inflow nozzle ends freely within the burner pot 18 above the brazier trough 27 at a height of approximately 15 centimeters above the surface.
- the inclination of the inlet connection 8 with respect to the horizontal is approximately between 25 and 35 °.
- the clear cross-sectional area of the inlet connection 8 is substantially larger than that of the oil supply line 7, which ends at the inlet connection 8.
- the inlet connector is also equipped with the same clear cross-sectional area from the inlet opening 51 to its bottom opening 50. The cross section of the opening does not narrow.
- the oil pumped by the oil pump 2 through the inlet opening 51 therefore flows primarily on the lower, inner lateral surface of the inlet connection, increasing in speed, down to the mouth 50. There it emerges and is broken up into fine droplets at the edge.
- This flow principle largely prevents incrustation or clogging of the inlet connector 8.
- the internal cavity of the inlet connector is in communication with the atmosphere. It is therefore not possible for the oil to flow back into the nozzle into the fuel line 6.
- a cleaning piston 52 which is displaceable within the nozzle cavity is provided, which, as shown in FIG. 6, has approximately the shape of a Maltese cross on average, with free spaces 54 being left between the arms 53 of the piston, through which the waste oil despite the installed piston can flow.
- the cleaning piston 52 is guided with a rod 55 out of a cover 56 of the connector 8 and ends in a knob 57.
- a helical spring 58 is installed between the knob and the cover. against the force of the spring 58, the piston 52 must be pressed inwards, and after each impression it automatically moves out again into the old position. This ensures that the area of the mouth 50 is always exposed.
- the Maltese cross shape of the piston is therefore chosen so that scrapers or cutting edges can be attached to the heads touching the inside of the inflow nozzle 8.
- the automatic program of the warm air heater is set so that the brazier is heated first before the first oil runs in. If, due to the high temperature of the brazier, automatic ignition usually occurs in the region of the trough, it must be ensured, however, that even waste oils with relatively high ignition levels can be reliably ignited.
- an ignition device 39 is provided, which is provided with an incandescent body 45, which is installed concentrically in the tubular housing of the ignition device 39.
- the filament consists of a perforated, ceramic tube with a built-in heating coil.
- the program control brings the incandescent body to red heat before the oil is admitted, so that the fuel-air mixture ignites immediately. The measures mentioned prevent the occurrence of smoke.
- the ignition can also be carried out with the aid of an infrared reflector igniter 46.
- a heating coil 48 is arranged within a reflector housing 47. The heat radiation is focused in the region of the trough 27 and also leads to an inflammatory point.
- an air line 49 to the reflector igniter 46, which directs a flow of combustion air onto the ignition area at the moment of ignition.
- the aforementioned devices serve to safely ignite the used oil.
- a photocell arrangement 24, which monitors the burning process is also installed, the associated photocell 25 essentially receiving the radiation emanating from the area of the trough 27 within the brazier.
- the photocell arrangement 24 takes over the continuous monitoring of the burning process.
- the photocell arrangement 24, which essentially consists of an eyepiece tube, is also provided with a cooling air nozzle 26 which is supplied with cooling air, which reaches the end of the eyepiece tube and also blows into the combustion area of the depression. This is ge ensured that the combustion area is always supplied with combustion air, so that as long as there is still unburned waste oil in the brazier 21, combustion is also maintained.
- the flame only extinguishes when there is no longer any combustible material, and this extinguishing is then also reliably observed by the photocell arrangement 24.
- the air flow is explained on the basis of FIGS. 1 and 7.
- the suction openings for the room air to be heated and that of the combustion air are located above the floor at a height of around 1.40 meters. This arrangement has been chosen so that no vapors of low-boiling organic compounds are sucked into the floor area, which could possibly lead to a deflagration within the combustion chamber volume.
- a suction opening 70 for the combustion air is shown in FIG. 7.
- the sucked-in air is fed to a combustion air blower 72, which presses the combustion air, metered according to the corresponding heat output, into the burner box.
- the air is distributed within the burner box and is pressed through the perforations 20 into the burner pot, where the combustion takes place or the fuel gases are generated.
- the caching combustion then takes place within the combustion chamber 30.
- the burned gases enter the heat exchanger 13 and leave it as exhaust gas through the exhaust pipe 35.
- the room air or the fresh air to be heated is attracted through a larger opening 74 in cross section and fed through a guide channel 75 to a warm air blower 76 which guides the air to be heated upwards through the heat exchanger 13 to the thawing elements heated by the exhaust gases.
- the heated air arrives through the head 77 of the thermal bath 10
- Different air outlets air outlet 78 in the upper area and a lower air outlet 79 in the lower area.
- the air duct is isolated by correspondingly insulated walls of the housing 11.
- the hot burner parts inside the device 10 are prevented from coming into contact with the outside world at all. Burning on the outer parts of the device is therefore not possible.
- FIG. 2 there is also a tank fill indicator 80 with a corresponding float 81 and an oil drain screw 82 on the sump 5.
- the brazier 18 including the additional heating device is arranged in a drawer 83 which can be pulled out relative to the housing.
- Another fuse is also provided for safe operation.
- the flame should go out and the oil supply is not interrupted, unburned fuel runs over the edge of the brazier 21 after a certain time.
- an overflow control sensor 87 is located in the lower part of the housing intended.
- the furnace function is controlled by an electronic control 58, which is attached to the side of the housing 11 in a switch box.
- the brazier 21 is empty. After switching on the hot air heater, the heating coil 23 and the high-temperature coil 28 are acted upon by heating current. They let the bowl heat up to a total temperature of around 400 ° C and in the bowl area to 800 ° C. With the help of the temperature sensor 37, the temperature of the brazier 21 is continuously monitored.
- the oil pump 2 is started. A thin stream of waste oil is brought into motion via the line and via the inlet connection 8 and flows in fine droplet form through the mouth 50 into the brazier 27.
- the ignition device 45 or 46 has also started to operate. The first drop that falls on the heated trough bursts there and is immediately vaporized intensively and briefly. As tests have shown, an ignition takes place immediately, so that the further waste oil flowing in is also set on fire immediately.
- the resistance wire coil 23 remains switched on during this first ignition process, but is kept at a lower temperature. The other, falling drops of oil burst and immediately come into intensive contact with the surface of the racing bowl. Since the ignition temperature has been exceeded, the fuel-air mixture located above the brazier ignites immediately. As soon as the photocell arrangement 24 has observed the ignition, the blower 72 is also switched on, which ensures a constant flow of combustion air.
- the flame emanating from the brazier has heated the brazier to such an extent that the combustion maintains itself. It is assumed that the brazier has a relatively high heat capacity due to its material.
- the oil pump 2 is switched off via a time delay relay and the fan 72 is also switched off after a further time delay.
- the ignition process can then be repeated after a certain time. Usually, however, an ignition Repeat required.
- the device 10 is switched off by interrupting the oil flow by switching off the oil pump 2. After a further time delay, the combustion air blower 72 is switched off. As long as there are flammable waste oil residues inside the bowl, they will be reduced by the small amounts of air created by the photo
- the resistance wire coil 23 is switched on and the pyrolyzing is initiated. After the combustion process had ended, a tough, solid bitumen slag had formed in the shell due to the relatively large amount of foreign substances in the waste oil, but this still largely contained carbon and other combustible substances.
- the resistance wire coil 23 heats the brazier up to a temperature of 600 to 700 ° C. The combustible residues are then pyrolyzed and burned on the heated pan. It can be seen that the solid bitumen slag disintegrates into residual dust during this pyrolysis process, which can be easily removed with the brazier after pulling out the box. The pyrolysis of the bituminous slag takes about five minutes. After this time, the coil 23 turns off again.
- the heating unit including the brazier is located in a drawer 23, this part of the device can be pulled out. Maintenance and repair door work is much easier.
- the device described above is suitable both for heating rooms and for generating steam or ice water. It can be kept in operation fully automatically. Their maintenance is largely problem-free. In particular, the ash quantities are reduced to a level not previously known in so-called waste oil stoves. During operation, it has also been shown that fly ash, which may contain environmentally harmful components of heavy metal, can be easily removed using filter devices.
- An intensive heat exchange is also carried out by the lamellar-coated jacket of the combustion chamber 30.
- These fins are made of copper, for example.
- the air outlet openings are adjustable in direction and intensity. According to measurements, the exhaust gas temperatures are around 180 to 200 ° C.
- the CO 2 content of the exhaust gases is measured at around 10% by volume. This results in an overall efficiency of 92%. Due to the meterability of the combustion air via the combustion air blower 72 and that of the waste oil via the oil pump 2, stoichiometric combustion can also be practically maintained. The soot content is extremely low. Only very small amounts of soot can be observed even at the beginning of the combustion process.
- the device can easily be operated up to an amount of 0.5 kg of waste oil per hour. With this small supply, only one entertainment flame is practically maintained in the brazier. Even with these low throughputs, stoichiometric conditions can still be maintained. It is possible to restart the power in a short time.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
- Feeding And Controlling Fuel (AREA)
- Processing Of Solid Wastes (AREA)
- Evaporation-Type Combustion Burners (AREA)
Description
Claims
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT82900545T ATE15104T1 (de) | 1981-02-17 | 1982-02-15 | Verfahren zur vorbereitung der reinigung der brennschale sowie vorrichtung zur verbrennung von rueckstandsreichen altoelen in einer brennschale. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE3105660A DE3105660C2 (de) | 1981-02-17 | 1981-02-17 | Vorrichtung zur Verbrennung von Brennölen, insbesondere von rückstandsreichen Altölen |
| DE3105660 | 1981-02-17 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0071626A1 true EP0071626A1 (de) | 1983-02-16 |
| EP0071626B1 EP0071626B1 (de) | 1985-08-21 |
Family
ID=6125017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP82900545A Expired EP0071626B1 (de) | 1981-02-17 | 1982-02-15 | Verfahren zur Vorbereitung der Reinigung der Brennschale sowie Vorrichtung zur Verbrennung von rückstandsreichen Altölen in einer Brennschale |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP0071626B1 (de) |
| JP (1) | JPS58500297A (de) |
| DE (2) | DE3105660C2 (de) |
| WO (1) | WO1982002933A1 (de) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3243395C2 (de) * | 1982-11-24 | 1985-07-25 | Danfoss A/S, Nordborg | Verdampfungsbrenner für flüssigen Brennstoff |
| FR2614398B1 (fr) * | 1987-04-27 | 1989-09-15 | Martel Antonin | Dispositif d'allumage automatique pour poele et tout chauffage a mazout par cuve a combustion |
| DE102008056798B4 (de) * | 2008-11-11 | 2012-02-02 | Wörle Umwelttechnik GmbH | Brennersystem und dessen Verwendung |
| AT527552A1 (de) * | 2023-08-28 | 2025-03-15 | Eta Heiztechnik Gmbh | Heizkessel |
Family Cites Families (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL246261A (de) * | ||||
| CH162285A (de) * | 1931-10-23 | 1933-06-15 | Ponsen Jacob | Verfahren zum Betrieb von Kelchbrennern für Ölverbrennung und zur Ausübung dieses Verfahrens eingerichteter Kelchbrenner. |
| FR889924A (fr) * | 1942-09-18 | 1944-01-24 | Guenet & Abbat | Perfectionnements aux réchauds, brûleurs ou similaires |
| US2538057A (en) * | 1943-12-06 | 1951-01-16 | William C Steele | Method of cleaning circulating heaters |
| US2479889A (en) * | 1946-08-09 | 1949-08-23 | Richard S Moore | Pot type oil burner with air preheating means |
| US2633189A (en) * | 1948-01-21 | 1953-03-31 | Richard M Pyle | Oil burner stove |
| FR1077939A (fr) * | 1953-05-30 | 1954-11-12 | Perfectionnements aux appareils de chauffage | |
| DE1030956B (de) * | 1954-03-23 | 1958-05-29 | Ammann & Co W | Geblaeselose Schalenbrennereinrichtung fuer Schweroelfeuerungen |
| US3102577A (en) * | 1960-04-05 | 1963-09-03 | Dekker Arien | Crude-oil burners |
| CH368255A (fr) * | 1961-03-22 | 1963-03-31 | Genton Rene | Fourneau pour combustible liquide |
| FR1388449A (fr) * | 1964-04-08 | 1965-02-05 | Robert Fischbach K G | Brûleur à évaporation pour combustibles liquides |
| AU411325B2 (en) * | 1967-03-20 | 1971-03-11 | Hecla Electrics Proprietary Limited | Improvements in or relating to oil heaters |
| JPS556642B1 (de) * | 1971-03-18 | 1980-02-19 | ||
| JPS4829277A (de) * | 1971-08-23 | 1973-04-18 | ||
| JPS4929451U (de) * | 1972-03-03 | 1974-03-13 | ||
| JPS5211700Y2 (de) * | 1972-07-26 | 1977-03-15 | ||
| GB1542056A (en) * | 1977-10-18 | 1979-03-14 | Kroll W | Combustion apparatus |
-
1981
- 1981-02-17 DE DE3105660A patent/DE3105660C2/de not_active Expired
-
1982
- 1982-02-15 EP EP82900545A patent/EP0071626B1/de not_active Expired
- 1982-02-15 JP JP57500656A patent/JPS58500297A/ja active Pending
- 1982-02-15 DE DE8282900545T patent/DE3265506D1/de not_active Expired
- 1982-02-15 WO PCT/EP1982/000028 patent/WO1982002933A1/de not_active Ceased
Non-Patent Citations (1)
| Title |
|---|
| See references of WO8202933A1 * |
Also Published As
| Publication number | Publication date |
|---|---|
| DE3105660A1 (de) | 1982-08-26 |
| WO1982002933A1 (en) | 1982-09-02 |
| DE3105660C2 (de) | 1983-11-03 |
| DE3265506D1 (en) | 1985-09-26 |
| EP0071626B1 (de) | 1985-08-21 |
| JPS58500297A (ja) | 1983-02-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE2836534C2 (de) | Verfahren zum Verbrennen flüssigen Brennstoffes und Brenner zur Durchführung des Verfahrens | |
| DE69500556T2 (de) | Kochgerät von Gas-Grill Typ | |
| DE3318637A1 (de) | Verdampfungs-oelbrenner | |
| DE2037434A1 (de) | Vorwarmer fur einen Motor | |
| EP0071626B1 (de) | Verfahren zur Vorbereitung der Reinigung der Brennschale sowie Vorrichtung zur Verbrennung von rückstandsreichen Altölen in einer Brennschale | |
| DE3218334C2 (de) | Heizvorrichtung | |
| DE2156374C3 (de) | Topfvergasungsbrenner für Flüssigkeitsbrennstoff | |
| DE2804968A1 (de) | Verfahren zum verbrennen fester brennstoffe, heizanlage zur durchfuehrung dieses verfahrens und verwendung der heizanlage | |
| DE20321670U1 (de) | Brenner für Pelletbrennstoff | |
| CH678652A5 (de) | ||
| DE69010168T2 (de) | Spiritusbrenner. | |
| DE363181C (de) | Verfahren zur Herstellung eines brennbaren Gases aus Wasserdampf und Daempfen von OEl | |
| AT139538B (de) | Vorrichtung zur Heizung mittels flüssigen Brennstoffes. | |
| AT139949B (de) | Vergaseranordnung für Feuerungen. | |
| DE3527057A1 (de) | Brennrost | |
| AT211937B (de) | Heizölbrenner mit einer in der Form eines endlosen Kanales ausgebildeten geschlossenen Verdampfungskammer | |
| CH438631A (de) | Heizungsanlage | |
| AT141343B (de) | Brenner für schwerflüssige Brennstoffe. | |
| DE648309C (de) | Brenner fuer fluessige Brennstoffe mit einem durch die Hauptflamme erhitzten Verdampfer | |
| CA1221012A (en) | Method and apparatus for the igniting or burning of combustible waste oils, in a combustion dish and method of preparing the cleaning of the combustion dish | |
| DE958948C (de) | Brenner mit einer zylindrischen Mischkammer | |
| DE2713279A1 (de) | Oelverdampfungsbrenner | |
| DE1679793C (de) | Durchlauferhitzer mit Olvergasungs brenner | |
| DE164214C (de) | ||
| DE3318634A1 (de) | Verdampfungs-oelbrenner |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| 17P | Request for examination filed |
Effective date: 19821011 |
|
| AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB LI LU NL SE |
|
| GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
| AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB LI LU NL SE |
|
| REF | Corresponds to: |
Ref document number: 15104 Country of ref document: AT Date of ref document: 19850915 Kind code of ref document: T |
|
| REF | Corresponds to: |
Ref document number: 3265506 Country of ref document: DE Date of ref document: 19850926 |
|
| ET | Fr: translation filed | ||
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19860228 |
|
| PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
| 26N | No opposition filed | ||
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 19870223 Year of fee payment: 6 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19870228 Year of fee payment: 6 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Effective date: 19880215 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Effective date: 19880216 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Effective date: 19880229 Ref country code: CH Effective date: 19880229 |
|
| BERE | Be: lapsed |
Owner name: ASBECK HEINZ Effective date: 19880228 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19880901 |
|
| NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee | ||
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19881028 |
|
| REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Effective date: 19881101 |
|
| GBPC | Gb: european patent ceased through non-payment of renewal fee | ||
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19881121 |
|
| REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Effective date: 19890228 |
|
| EUG | Se: european patent has lapsed |
Ref document number: 82900545.3 Effective date: 19880927 |