EP0446435B1 - Device for burning oxidizable components in exhaust air - Google Patents
Device for burning oxidizable components in exhaust air Download PDFInfo
- Publication number
- EP0446435B1 EP0446435B1 EP90123052A EP90123052A EP0446435B1 EP 0446435 B1 EP0446435 B1 EP 0446435B1 EP 90123052 A EP90123052 A EP 90123052A EP 90123052 A EP90123052 A EP 90123052A EP 0446435 B1 EP0446435 B1 EP 0446435B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- heat
- chamber
- container
- heat exchanger
- socket
- 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.)
- Expired - Lifetime
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
- F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
- F23G7/066—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator
Definitions
- the invention relates to a device for burning oxidizable constituents contained in an exhaust air stream from a cylindrical container with a feed nozzle and a discharge nozzle.
- the feed connector opens into a distribution space, to which the inlet-side legs of radially angled heat exchanger tubes are connected. These extend over a substantial part of the length of the container and open into an annular chamber adjacent to an end face of the container and opposite the distribution space.
- This surrounds a concentrically arranged burner, coaxially opposite a flue gas mixing pipe.
- This is connected by a main combustion chamber surrounding it to an annular space which in turn surrounds it and which receives the heat exchanger tubes and to which the discharge pipe is connected.
- Such a device is known from DE-A-35 32 232. Since the preheating temperature of the exhaust air loaded with oxidizable components should be brought as close as possible to the combustion chamber temperature, there are high demands on the ability to compensate for changes in length, particularly under dynamic conditions, i.e. changes in temperature, volume flow and contaminant loading in the exhaust air Heat exchanger tubes. If the device is also to be operated with only a very low partial exhaust air flow, even heat exchanger tubes with laminar flow are located directly next to heat exchanger tubes with turbulent flow. The resulting different heat transfer on the tube walls inevitably leads to different tube wall temperatures, with the result that even immediately adjacent heat exchanger tubes experience different elongations.
- the heat exchanger tubes are bent outwards with their colder legs on the inflow side, the exhaust air flowing outside the heat exchanger tubes being freed of the oxidizable components is guided over the pipe bends and the bent pipe sections.
- the legs of the heat exchanger tubes which are bent outwards, have to be arranged with the smallest possible diameter.
- the combustion chamber insofar as it is embedded within the heat exchanger, only has a very small volume, ie that (the main part of the combustion chamber or) a large part of the entire combustion chamber outside of the area enclosed by the heat exchanger tubes is to be arranged, whereby the length of the container inevitably increases significantly.
- the radial legs of the heat exchanger tubes arranged on the outside can only be made relatively short, so that they, when welded into the outer wall of the container, behave too rigidly to be able to compensate for any significant expansion. Due to the shortness of the pipe legs bent outwards, these are at most suitable to compensate for differences in expansion of the pipes with one another, but not also the differences in expansion between the complete tube bundle formed from the heat exchanger tubes on the one hand and the jacket surrounding the tube bundle on the other. Therefore, a further main compensator must be provided in the known device, which makes the device considerably more expensive.
- the invention has for its object to provide a device of the type described above, which is characterized by a compact design and in which each heat exchanger tube can still experience significant changes in length without having to overcome significant adjustment forces.
- the length of these legs can be chosen so large, even with a relatively small container diameter, depending on the diameter of the cylindrical jacket that encloses the distribution space, that each heat exchanger tube has a considerable compensation capacity with regard to its thermal expansion disposes.
- the jacket diameter of the distribution space arranged concentrically to the container axis can be dimensioned so small that the size of the jacket surface is just sufficient to weld all the upstream legs of the heat exchanger tubes to the jacket.
- the feed connector is also coaxial to the container axis. This results in the aerodynamically favorable training possibility that the feed pipe merges smoothly into the cylindrical jacket of the distribution space.
- a bypass is provided in an end face of the distribution space, coaxial with the latter, which consists of a pipe socket protruding into the flue gas mixing pipe.
- the device according to the invention makes it possible to equip it with such a bypass, which is preferably only required for a certain operating mode, with little effort, if necessary also retrospectively.
- the device essentially consists of a cylindrical container 1, which is provided on the outside with a heat-insulating insulation 2.
- the container 1 is provided on one end face 3 with a feed connector 4 arranged coaxially to the container axis and opening into a cylindrical distribution chamber 5.
- the feed pipe 4 and the distribution chamber 5 have a matching diameter and therefore merge into one another continuously.
- heat exchanger tubes 7 In a jacket 6 of the distribution chamber 5, inflow ends of heat exchanger tubes 7 are welded.
- the heat exchanger tubes 7, which are cylindrical near the wall of the container 1 are arranged and in this respect extend axially over a substantial part of the length of the container 1, each with an inlet-side leg 8 bent radially inwards.
- the outlet-side ends of the heat exchanger tubes 7 open into an annular chamber 9 which adjoins an end face 10 of the container 1.
- the end face 10 carries a burner 11 which is arranged concentrically to the annular chamber 9 and which opens into a flue gas mixing tube 12. This ends at a distance from a partition wall 13 which covers the distribution chamber 5 and delimits a main combustion chamber 14 on the end face.
- the main combustion chamber 14 surrounds the flue gas mixing tube 12 and communicates with an annular space 16 via a deflection space 15.
- the heat exchanger tubes 7 are accommodated, which also penetrate the deflection space 15 and are firmly inserted into an annular disk 17 that delimits the end face.
- the annular space 16 is connected to a discharge connection 18 which is radially connected to the casing of the container 1.
- a bypass 19 is provided concentrically in the partition 13, which consists of an end face closed, provided with radial bores 20 and protruding into the high-speed pipe 12 pipe socket 21.
- the bypass 19 can be released or closed more or less depending on the position of a flap 22 in the pipe socket 21.
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Exhaust Gas After Treatment (AREA)
- Combustion Of Fluid Fuel (AREA)
- Telephone Function (AREA)
- Cylinder Crankcases Of Internal Combustion Engines (AREA)
- Incineration Of Waste (AREA)
Abstract
Description
Die Erfindung betrifft eine Vorrichtung zum Verbrennen von in einem Abluftstrom enthaltenen oxidierbaren Bestandteilen aus einem zylindrischen Behälter mit einem Zuführstutzen und einem Abführstutzen. Der Zuführstutzen mündet in einen Verteilraum, an den die eintrittsseitigen Schenkel von radial abgewinkelten Wärmetauscherrohren angeschlossen sind. Diese erstrecken sich über einen wesentlichen Teil der Länge des Behälters und münden in eine einer Stirnseite des Behälters benachbarte und dem Verteilraum gegenüberliegende Ringkammer. Diese umschließt einen konzentrisch angeordneten Brenner, dem koaxial ein Rauchgasmischrohr gegenüberliegt. Dieses ist durch eine es umschließende Hauptbrennkammer mit einem diese wiederum umschließenden Ringraum verbunden, der die Wärmetauscherrohre aufnimmt und an den der Abführstutzen angeschlossen ist.The invention relates to a device for burning oxidizable constituents contained in an exhaust air stream from a cylindrical container with a feed nozzle and a discharge nozzle. The feed connector opens into a distribution space, to which the inlet-side legs of radially angled heat exchanger tubes are connected. These extend over a substantial part of the length of the container and open into an annular chamber adjacent to an end face of the container and opposite the distribution space. This surrounds a concentrically arranged burner, coaxially opposite a flue gas mixing pipe. This is connected by a main combustion chamber surrounding it to an annular space which in turn surrounds it and which receives the heat exchanger tubes and to which the discharge pipe is connected.
Eine derartige Vorrichtung ist aus der DE-A- 35 32 232 bekannt. Da die Vorheiztemperatur der mit oxidierbaren Bestandteilen beladenen Abluft möglichst in die Nähe der Brennkammertemperatur gebracht werden soll, ergeben sich insbesondere unter dynamischen Bedingungen, d.h. Veränderungen hinsichtlich Temperatur, Volumenstrom und Störstoffbeladung der Abluft, hohe Anforderungen an die Kompensationsfähigkeit von Längenänderungen der Wärmetauscherrohre. Soll die Vorrichtung auch mit nur einem sehr geringen Abluftteilstrom betrieben werden, liegen sogar Wärmetauscherrohre mit laminarer Beströmung unmittelbar neben Wärmetauscherrohren mit turbulenter Beströmung. Der daraus resultierende unterschiedliche Wärmeübergang an den Rohrwandungen führt zwangsläufig zu unterschiedlichen Rohrwandtemperaturen mit der Folge, daß sogar unmittelbar benachbarte Wärmetauscherrohre unterschiedliche Längendehnungen erfahren.Such a device is known from DE-A-35 32 232. Since the preheating temperature of the exhaust air loaded with oxidizable components should be brought as close as possible to the combustion chamber temperature, there are high demands on the ability to compensate for changes in length, particularly under dynamic conditions, i.e. changes in temperature, volume flow and contaminant loading in the exhaust air Heat exchanger tubes. If the device is also to be operated with only a very low partial exhaust air flow, even heat exchanger tubes with laminar flow are located directly next to heat exchanger tubes with turbulent flow. The resulting different heat transfer on the tube walls inevitably leads to different tube wall temperatures, with the result that even immediately adjacent heat exchanger tubes experience different elongations.
Um mit konstruktiv einfachen Mitteln den Wärmetauscherrohren insbesondere eine temperaturbedingte Ausdehnung zu ermöglichen und sie dadurch vor Schäden zu sichern, sind bei der bekannten Vorrichtung die Wärmetauscherrohre mit ihren kälteren einströmseitigen Schenkeln nach außen gebogen, wobei die außerhalb der Wärmetauscherrohre strömende, von den oxidierbaren Bestandteilen befreite Abluft über die Rohrbögen und die abgebogenen Rohrabschnitte geführt wird.In order to enable the heat exchanger tubes to expand, in particular with temperature, with structurally simple means and thereby protect them from damage, in the known device the heat exchanger tubes are bent outwards with their colder legs on the inflow side, the exhaust air flowing outside the heat exchanger tubes being freed of the oxidizable components is guided over the pipe bends and the bent pipe sections.
Wenn bei der bekannten Vorrichtung relativ große Behälterdurchmesser vermieden werden sollen, müssen mit Rücksicht auf die nach außen gebogenen Schenkel der Wärmetauscherrohre diese im übrigen auf einem möglichst kleinen Durchmesser angeordnet werden. Die Folge davon ist, daß der Brennraum, soweit er innerhalb des Wärmetauschers eingebettet ist, nur ein sehr kleines Volumen bekommt, d. h. daß (der Hauptteil des Brennraums bzw.) ein großer Teil des gesamten Brennraums außerhalb des von den Wärmetauscherrohren umschlossenen Bereichs anzuordnen ist, wodurch sich die Länge des Behälters zwangsläufig erheblich vergrößert. Zudem können bei nach außen gebogenen Wärmetauscherrohren die radialen Schenkel der außen angeordneten Wärmetauscherrohre nur verhältnismäßig kurz ausgebildet werden, so daß diese sich, eingeschweißt in die äußere Wandung des Behälters, zu starr verhalten, um eine nennenswerte Dehnung kompensieren zu können. Bedingt durch die Kürze der nach außen abgebogenen Rohrschenkel sind diese allenfalls geeignet, Dehnungsunterschiede der Rohre untereinander auszugleichen, nicht aber auch noch die Dehnungsunterschiede zwischen dem aus den Wärmetauscherrohren gebildeten vollständigen Rohrbündel einerseits und dem das Rohrbündel umgebenden Mantel andererseits. Deshalb muß dazu bei der bekannten Vorrichtung zusätzlich ein weiterer Hauptkompensator vorgesehen werden, der die Vorrichtung erheblich verteuert.If, in the known device, relatively large container diameters are to be avoided, the legs of the heat exchanger tubes, which are bent outwards, have to be arranged with the smallest possible diameter. The consequence of this is that the combustion chamber, insofar as it is embedded within the heat exchanger, only has a very small volume, ie that (the main part of the combustion chamber or) a large part of the entire combustion chamber outside of the area enclosed by the heat exchanger tubes is to be arranged, whereby the length of the container inevitably increases significantly. In addition, in the case of heat exchanger tubes which are bent outwards, the radial legs of the heat exchanger tubes arranged on the outside can only be made relatively short, so that they, when welded into the outer wall of the container, behave too rigidly to be able to compensate for any significant expansion. Due to the shortness of the pipe legs bent outwards, these are at most suitable to compensate for differences in expansion of the pipes with one another, but not also the differences in expansion between the complete tube bundle formed from the heat exchanger tubes on the one hand and the jacket surrounding the tube bundle on the other. Therefore, a further main compensator must be provided in the known device, which makes the device considerably more expensive.
Der Erfindung liegt die Aufgabe zugrunde, eine Vorrichtung der eingangs beschriebenen Art vorzuschlagen, die sich durch eine kompakte Bauweise auszeichnet und bei der trotzdem jedes Wärmetauscherrohr erhebliche Längenänderungen erfahren kann, ohne daß dazu nennenswerte Verstellkräfte überwunden werden müssen.The invention has for its object to provide a device of the type described above, which is characterized by a compact design and in which each heat exchanger tube can still experience significant changes in length without having to overcome significant adjustment forces.
Zur Losung dieser Aufgabe wird von einer Vorrichtung der im Oberbegriff des Anspruchs 1 genannten gattungsgemäßen Art ausgegangen, welche erfindungsgemäß die im kennzeichnenden Teil desselben angegebenen Merkmale aufweist.To solve this problem, a device of the generic type mentioned in the preamble of
Durch die erfindungsgemäß radial nach innen abgewinkelten eintrittsseitigen Schenkel der Wärmetauscherrohre kann die Länge dieser Schenkel auch bei einem verhältnismäßig kleinen Behälterdurchmesser in Abhängigkeit vom Durchmesser des zylindrischen Mantels, der den Verteilraum umschließt, so groß gewählt werden, daß jedes Wärmetauscherrohr über ein erhebliches Kompensationsvermögen hinsichtlich seiner Wärmeausdehnung verfügt.Due to the radially inward angled inlet side legs of the heat exchanger tubes according to the invention, the length of these legs can be chosen so large, even with a relatively small container diameter, depending on the diameter of the cylindrical jacket that encloses the distribution space, that each heat exchanger tube has a considerable compensation capacity with regard to its thermal expansion disposes.
Der Manteldurchmesser des konzentrisch zur Behälterachse angeordneten Verteilraums kann so klein bemessen werden, daß die Größe der Mantelfläche gerade noch ausreicht, um sämtliche einströmseitigen Schenkel der Wärmetauscherrohre am Mantel anzuschweißen. So wie der Verteilraum konzentrisch zur Behälterachse angeordnet ist, befindet sich auch der Zuführstutzen koaxial zur Behälterachse. Dadurch ergibt sich die strömungstechnisch günstige Ausbildungsmöglichkeit, daß der Zuführstutzen stufenlos in den zylindrischen Mantel des Verteilraums übergeht.The jacket diameter of the distribution space arranged concentrically to the container axis can be dimensioned so small that the size of the jacket surface is just sufficient to weld all the upstream legs of the heat exchanger tubes to the jacket. Just as the distribution space is arranged concentrically to the container axis, the feed connector is also coaxial to the container axis. This results in the aerodynamically favorable training possibility that the feed pipe merges smoothly into the cylindrical jacket of the distribution space.
Nach einer besonders vorteilhaften Ausgestaltung der Erfindung ist in einer Stirnseite des Verteilraums zu dieser koaxial ein Bypass vorgesehen, der aus einem in das Rauchgasmischrohr hineinragenden Rohrstutzen besteht.According to a particularly advantageous embodiment of the invention, a bypass is provided in an end face of the distribution space, coaxial with the latter, which consists of a pipe socket protruding into the flue gas mixing pipe.
Die erfindungsgemäße Vorrichtung ermöglicht es, diese mit geringem Aufwand, im Bedarfsfalle auch nachträglich, mit einem solchen Bypass auszurüsten, der vorzugsweise nur bei einer bestimmten Betriebsweise erforderlich ist.The device according to the invention makes it possible to equip it with such a bypass, which is preferably only required for a certain operating mode, with little effort, if necessary also retrospectively.
In der Zeichnung ist ein Ausführungsbeipiel einer erfindungsgemäßen Vorrichtung in einem Längsschnitt dargestellt:In the drawing, an exemplary embodiment of a device according to the invention is shown in a longitudinal section:
Die Vorrichtung besteht im wesentlichen aus einem zylinderförmigen Behälter 1, der außenseitig mit einer wärmedämmenden Isolierung 2 versehen ist.The device essentially consists of a
Der Behälter 1 ist auf einer Stirnseite 3 mit einem koaxial zur Behälterachse angeordneten Zuführstutzen 4 versehen, der in eine zylindrische Verteilkammer 5 mündet. Der Zuführstutzen 4 und die Verteilkammer 5 haben einen übereinstimmenden Durchmesser und gehen daher stufenlos ineinander über.The
In einem Mantel 6 der Verteilkammer 5 sind einströmseitige Enden von Wärmetauscherrohren 7 eingeschweißt. Dazu sind die Wärmetauscherrohre 7, die in Wandnähe des Behälters 1 zylinderförmig angeordnet sind und sich insoweit axial über einen wesentlichen Teil der Länge des Behälters 1 erstrecken, jeweils mit einem eintrittsseitigen Schenkel 8 radial nach innen gebogen.In a
Die austrittsseitigen Enden der Wärmetauscherrohre 7 münden in eine Ringkammer 9, die an eine Stirnseite 10 des Behälters 1 angrenzt. Die Stirnseite 10 trägt einen konzentrisch zur Ringkammer 9 angeordneten Brenner 11, der in ein Rauchgasmischrohr 12 mündet. Dieses endet in einem Abstand zu einer Trennwand 13, welche die Verteilkammer 5 abdeckt und eine Hauptbrennkammer 14 stirnseitig begrenzt.The outlet-side ends of the
Die Hauptbrennkammer 14 umschließt das Rauchgasmischrohr 12 und steht über einen Umlenkraum 15 mit einem Ringraum 16 in Verbindung.The
Im Ringraum 16 sind die Wärmetauscherrohre 7 untergebracht, die auch den Umlenkraum 15 durchdringen und in eine diese stirnseitig begrenzende Ringscheibe 17 fest eingefügt sind.In the
Untereinander unterschiedliche Längenänderungen der Wärmetauscherrohre 7 infolge unterschiedlicher Rohrtemperaturen werden dadurch kompensiert, daß sich die Winkel, welche die verhältnismäßig langen Schenkel 8 mit dem übrigen Verlauf der Wärmetauscherrohre 7 einschließen, entsprechend ändern, wozu geringfügige Dehnungskräfte ausreichen, so daß nennenswerte Druck-, Zug- oder Biegebeanspruchungen in den Wärmetauscherrohren 7 und entsprechende Beanspruchungen an deren Einfügestellen verhindert sind.Different length changes of the
Der Ringraum 16 steht mit einem am Mantel des Behälters 1 radial angeschlossenen Abführstutzen 18 in Verbindung.The
Um wahlweise einen Teil des mit oxidierbaren Bestandteilen beladenen Abgases unter Umgehung der Wärmetauscherrohre 7, des Brenners 11 und des wesentlichsten Teils des Rauchgasmischrohrs 12 im Kurzschluß in den inneren Ringraum 14 einzuleiten, ist konzentrisch in der Trennwand 13 ein Bypass 19 vorgesehen, der aus einem stirnseitig verschlossenen, mit radialen Bohrungen 20 versehenen und in das Hochgeschwindigkeitsrohr 12 hineinragenden Rohrstutzen 21 besteht. Der Bypass 19 ist in Abhängigkeit von der Stellung einer Klappe 22 im Rohrstutzen 21 mehr oder weniger freigebbar bzw. verschließbar.In order to selectively introduce a portion of the exhaust gas loaded with oxidizable constituents, bypassing the
Claims (3)
- Device for combustion of oxidizable matter contained in an exhaust flow, comprising a cylindrical container (1) with a feed socket (4) and an outlet socket (18), wherein the feed socket (4) terminates in a distributor chamber (5) to which are connected the input shanks (8) of radially angled heat-exchanger tubes (7), which extend over a substantial part of the container's length and terminate in a circular chamber chamber (9), which is adjacent an end (10) of the container (1) and opposite the distributor chamber (5) and comprises a concentrically arranged burner (11), opposite which is coaxially located a flue-gas mixer pipe (12), which is connected by its surrounding main combustion chamber (14) to a circular area (16), which encloses the latter and accommodates the heat-exchanger pipes (7) and to which are connected the outlet sockets (18), characterised in that the inlet shanks (8) of the heat-exchanger pipes (7) are angled inwardly and that their ends are inserted into a cylindrical casing (6) which concentrically encloses the distributor chamber (5), and that the distributor chamber (5) and the feed socket (4) are arranged coaxially to the axis of the container (1).
- Device according to claim 1, characterised in that the feed socket (4) merges without steps into the cylindrical casing (6) of the distributor chamber (5).
- Device according to claim 1 or 2, characterised in that in one end (13) of the distributor chamber (5) is provided, coaxially thereto, a bypass (19) out of a pipe socket (21) which intrudes into the high-speed pipe (12)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT90123052T ATE89907T1 (en) | 1990-03-10 | 1990-12-01 | DEVICE FOR COMBUSTING OXIDIZABLE COMPONENTS CONTAINED IN AN EXHAUST AIR STREAM. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4007625 | 1990-03-10 | ||
| DE4007625 | 1990-03-10 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP0446435A2 EP0446435A2 (en) | 1991-09-18 |
| EP0446435A3 EP0446435A3 (en) | 1992-03-04 |
| EP0446435B1 true EP0446435B1 (en) | 1993-05-26 |
Family
ID=6401878
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP90123052A Expired - Lifetime EP0446435B1 (en) | 1990-03-10 | 1990-12-01 | Device for burning oxidizable components in exhaust air |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US5200155A (en) |
| EP (1) | EP0446435B1 (en) |
| AT (1) | ATE89907T1 (en) |
| CA (1) | CA2037863C (en) |
| DE (1) | DE59001568D1 (en) |
Families Citing this family (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5309849A (en) * | 1992-05-22 | 1994-05-10 | Andritz Tcw Engineering Gmbh | Sludge drying system with recycling exhaust air |
| US5556273A (en) * | 1994-10-28 | 1996-09-17 | Tuscaloosa Steel Corporation | Combustion system for a steckle mill |
| US5558029A (en) * | 1994-12-14 | 1996-09-24 | Barnstead/Thermlyne Corporation | Ashing furnace and method |
| US5643544A (en) * | 1995-04-28 | 1997-07-01 | Applied Web Systems, Inc. | Apparatus and method for rendering volatile organic compounds harmless |
| US6000935A (en) * | 1997-02-21 | 1999-12-14 | Troxler Electronic Laboratories, Inc | Adjustable apparatus for pyrolysis of a composite material and method of calibration therefor |
| US5735680A (en) * | 1997-03-13 | 1998-04-07 | Applied Web Systems, Inc. | Fume incineration |
| US6269755B1 (en) * | 1998-08-03 | 2001-08-07 | Independent Stave Company, Inc. | Burners with high turndown ratio |
| KR100523752B1 (en) * | 2001-12-05 | 2005-10-24 | 송권규 | high temperature gas reforming cyclo-incinerator |
| DE102004051491B3 (en) * | 2004-07-27 | 2006-03-02 | Eisenmann Maschinenbau Gmbh & Co. Kg | Thermal post-combustion device and method for operating such |
| IE20070094A1 (en) * | 2007-02-15 | 2008-12-10 | Francis Donal Duignan | A combustion chamber for burning solid fuels |
| WO2011142811A1 (en) * | 2010-05-11 | 2011-11-17 | Anglo American Holding, Llc. | A recuperated combustion apparatus assembly with steam injection |
| DE102013203448A1 (en) * | 2013-02-28 | 2014-08-28 | Dürr Systems GmbH | Plant and method for treating and / or utilizing gaseous medium |
| GB2544520A (en) * | 2015-11-19 | 2017-05-24 | Edwards Ltd | Effluent gas treatment apparatus and method |
| CN110566982B (en) * | 2019-10-10 | 2020-11-03 | 江苏中矿贝莱柯环境科技有限公司 | Combustion device for waste gas environment-friendly treatment |
| CN113531565B (en) * | 2021-09-14 | 2021-12-10 | 江苏中科机械有限公司 | Cleaning device of RTO heat accumulation formula waste gas oxidation stove |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1140958B (en) * | 1957-09-20 | 1962-12-13 | Yuba Cons Ind Inc | Vertical heater for gases with a cylindrical combustion chamber and tubes arranged in a single circle |
| FR1199130A (en) * | 1958-06-13 | 1959-12-11 | Electricite De France | Improvements to tubular heat exchangers |
| US3549333A (en) * | 1968-07-23 | 1970-12-22 | Universal Oil Prod Co | Recuperative form of direct thermal incinerator |
| DE3014269C2 (en) * | 1980-04-14 | 1982-11-25 | Katec, Katalytische Lufttechnik Betz Gmbh & Co, 6467 Hasselroth | Incinerator for the incineration of contaminants in exhaust air and waste substances |
| DE3532232A1 (en) * | 1985-09-10 | 1987-03-19 | Katec Betz Gmbh & Co | DEVICE FOR BURNING OXIDISABLE COMPONENTS IN A CARRIER GAS |
-
1990
- 1990-12-01 EP EP90123052A patent/EP0446435B1/en not_active Expired - Lifetime
- 1990-12-01 DE DE9090123052T patent/DE59001568D1/en not_active Expired - Fee Related
- 1990-12-01 AT AT90123052T patent/ATE89907T1/en not_active IP Right Cessation
-
1991
- 1991-03-08 CA CA002037863A patent/CA2037863C/en not_active Expired - Fee Related
- 1991-03-11 US US07/667,514 patent/US5200155A/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| DE59001568D1 (en) | 1993-07-01 |
| CA2037863C (en) | 2001-09-11 |
| CA2037863A1 (en) | 1991-09-11 |
| US5200155A (en) | 1993-04-06 |
| EP0446435A3 (en) | 1992-03-04 |
| ATE89907T1 (en) | 1993-06-15 |
| EP0446435A2 (en) | 1991-09-18 |
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