EP0447631B1 - Dispositif de combustion pour impuretés - Google Patents

Dispositif de combustion pour impuretés Download PDF

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Publication number
EP0447631B1
EP0447631B1 EP90123045A EP90123045A EP0447631B1 EP 0447631 B1 EP0447631 B1 EP 0447631B1 EP 90123045 A EP90123045 A EP 90123045A EP 90123045 A EP90123045 A EP 90123045A EP 0447631 B1 EP0447631 B1 EP 0447631B1
Authority
EP
European Patent Office
Prior art keywords
heat
container
media flow
pipes
exchanger
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
Application number
EP90123045A
Other languages
German (de)
English (en)
Other versions
EP0447631A2 (fr
EP0447631A3 (en
Inventor
Ernst Dipl.-Ing. Wirl
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
H Krantz GmbH and Co
Original Assignee
H Krantz GmbH and Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by H Krantz GmbH and Co filed Critical H Krantz GmbH and Co
Priority to AT90123045T priority Critical patent/ATE102327T1/de
Publication of EP0447631A2 publication Critical patent/EP0447631A2/fr
Publication of EP0447631A3 publication Critical patent/EP0447631A3/de
Application granted granted Critical
Publication of EP0447631B1 publication Critical patent/EP0447631B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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 contaminants contained in a media stream.
  • the device consists of a cylindrical container with an inlet connection and an outlet connection for the media flow. This can be introduced into an annular chamber by means of radially extending bundles of heat exchanger tubes arranged inside the container. This surrounds a burner arranged on an inside face of the container and merges into a high-speed tube arranged coaxially with the burner.
  • the high-speed pipe is connected to an inner annular space surrounding it, from which the media flow can be fed to the outlet connection via the heat exchanger pipes.
  • the end regions of the heat exchanger tubes on the inflow side are bent radially outward and are washed around by the heated media stream treated.
  • Such a device is known from DE-A-35 32 232.
  • a corresponding device known from EP-A-0 040 690 in which the heat exchanger tubes on the hot side of the device, that is to say in the region of the burner, are bent inwards and inserted in a drum concentrically surrounding the burner outward bent heat exchanger tubes the advantage that the tube ends on a much larger Circumferential surface can be arranged so that easier welding is achieved.
  • the welded ends can be at a considerably greater distance from one another, so that the jacket receiving the ends does not have to be an additional component such as a drum, but instead the inner wall of an outer annular space can be used as a fastening surface through which the carrier gas containing the oxidizable components can be used Entry opening is guided to the heat exchanger tubes.
  • the invention has for its object to provide a device of the type described in the introduction, in which all heat exchanger tubes have the same bending and compensating capacity, the force acting on each tube should be as low as possible, which is also a prerequisite for damaging oscillation of pipes is avoided.
  • all radii of the bends and the connecting pieces between the bends of all heat exchanger tubes can be dimensioned the same, so that all heat exchanger tubes also have mutually matching compensation properties.
  • the connecting pieces between the arcs of the heat exchanger tubes are aligned tangentially to a circle, the center of which lies in the central axis of the container.
  • this configuration enables the use of heat exchanger tubes with relatively long connecting pieces between the bends with the same device dimensions, so that the flexibility of the heat exchanger tubes can be increased considerably.
  • 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 in the vicinity of an end face 3 with a radially penetrating the container wall Provided inlet port 4, which opens into an annular prechamber 5. This is delimited on its side facing the center of the container by a circular disk 6, through which the inflow ends of heat exchanger tubes 7 are passed.
  • the heat exchanger tubes 7, which are arranged cylindrically near the wall of the container 1 and extend axially over a substantial part of the container length, are each provided with two bends 8 at the inflow-side end region, which form a Z- or S-shaped double bend 8-8 via a connecting piece 9.
  • the inflow-side end of a heat exchanger tube 7 lies on a larger radius than its outflow-side end, which penetrates a partition 10. This is arranged at a distance from an end face 11 of the container 1, whereby an annular chamber 12 is divided into which the outlet-side ends of the heat exchanger tubes 7 open.
  • the ends of the heat exchanger tubes 7 are welded rigidly on the inflow side to the circular disk 6, which in turn is rigidly arranged, and are also rigidly welded on the outflow side to the dividing wall 10, which is likewise rigidly arranged. Every change in length of the heat exchanger tubes 7 as a result of temperature changes is completely compensated for by a corresponding deformation of the S- or Z-shaped double bends 8-8.
  • the deformability of the double arches 8-8 is the greater and the more so done more elastic, the greater the length of the connecting pieces 9.
  • the annular space 12 encloses a burner 13, which is arranged concentrically with the end face 11 and opens into a coaxial high-speed tube 14. This in turn opens into a swirling chamber 15 which is delimited by the end face 3.
  • the swirling chamber 15 is adjoined in the exit plane of the high-speed tube 14 by an inner annular space 16 which surrounds the high-speed tube 14 and extends over the most essential part of its length before it opens into an annular deflection space 17.
  • An outer annular space 18, which contains the heat exchanger tubes 7, is connected to this.
  • the outer annular space 18 extends with a radially widened end piece 19, in which the double bends 8-8 of the heat exchanger tubes 7 are accommodated, into an area which partially surrounds the swirl chamber 15.
  • an outlet connection 20 is connected radially, which likewise penetrates the container wall in the vicinity of the inlet connection 4 and is arranged parallel to the latter.

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)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Regulation And Control Of Combustion (AREA)

Claims (2)

  1. Dispositif de combustion pour des impuretés contenues dans un courant de fluides, constitué par un réservoir (1) cylindrique pourvu d'un raccord d'admission (4) et d'un raccord d'évacuation (20) pour le courant de fluides qui peut être envoyé dans une chambre annulaire (12) à travers des faisceaux de tuyaux d'échange thermique (7) disposés de manière cylindrique dans une chambre annulaire externe (18) du réservoir et s'étendant de manière radiale, laquelle chambre annulaire (18) entoure un brûleur (13) situé au niveau d'une face intérieure frontale (11) du réservoir (1) et se transforme, en direction de la face opposée, en un tube à grande vitesse (14) disposé de manière coaxiale au brûleur (13), lequel tube à grande vitesse communique avec une chambre annulaire interne (16) qui l'entoure, à partir de laquelle le courant de fluides peut être envoyé dans le raccord d'évacuation (20) en passant autour des tuyaux d'échange thermique (7), les zones d'extrémités des tuyaux d'échange thermique (7) situées du côté de l'admission étant coudées vers l'extérieur et baignées par le courant de fluides chauffé que l'on traite, ce dispositif étant caractérisé par le fait que chaque tuyau d'échange thermique (7) est pourvu, au niveau de sa zone d'extrémité située du côté de l'admission, de deux coudes (8) qui forment, par l'intermédiaire d'une pièce de raccord (9) située entre eux, un raccord à double courbure (8-8) en forme de Z ou de S, qui forme ainsi une extrémité de tuyau disposée en parallèle au reste de ce tuyau d'échange thermique (7) et qui traverse une paroi de séparation (6) circulaire, et par le fait que ces zones d'extrémités des tuyaux d'échange thermique (7) sont disposées dans une partie d'extrémité (19) élargie radialement par rapport à une chambre annulaire externe (18), et que le raccord d'évacuation (20) est contigu à cette partie d'extrémité (19).
  2. Dispositif selon la revendication 1, caractérisé par le fait que les pièces de raccord (9) situées entre les coudes (8-8) des tuyaux d'échange thermique (7), sont orientées de manière tangentielle à un cercle dont le centre se trouve sur l'axe du réservoir (1).
EP90123045A 1990-03-10 1990-12-01 Dispositif de combustion pour impuretés Expired - Lifetime EP0447631B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT90123045T ATE102327T1 (de) 1990-03-10 1990-12-01 Vorrichtung zum verbrennen von stoerstoffen.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE4007626 1990-03-10
DE4007626 1990-03-10

Publications (3)

Publication Number Publication Date
EP0447631A2 EP0447631A2 (fr) 1991-09-25
EP0447631A3 EP0447631A3 (en) 1992-03-11
EP0447631B1 true EP0447631B1 (fr) 1994-03-02

Family

ID=6401879

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90123045A Expired - Lifetime EP0447631B1 (fr) 1990-03-10 1990-12-01 Dispositif de combustion pour impuretés

Country Status (4)

Country Link
EP (1) EP0447631B1 (fr)
AT (1) ATE102327T1 (fr)
CA (1) CA2037864A1 (fr)
DE (1) DE59004810D1 (fr)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0702195A3 (fr) * 1994-08-17 1997-05-14 Grace W R & Co Distributeur d'air annulaire pour système d'oxydation thermique à régénération de chaleur
US5601789A (en) * 1994-12-15 1997-02-11 W. R. Grace & Co.-Conn. Raw gas burner and process for burning oxygenic constituents in process gas
US5618173A (en) * 1994-12-15 1997-04-08 W.R. Grace & Co.-Conn. Apparatus for burning oxygenic constituents in process gas
US5762880A (en) * 1996-12-16 1998-06-09 Megtec Systems, Inc. Operational process and its improved control system of a secondary air burner
CN110566982B (zh) * 2019-10-10 2020-11-03 江苏中矿贝莱柯环境科技有限公司 一种废气环保处理用燃烧装置

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2218528B1 (fr) * 1973-02-19 1977-12-30 Stein Industrie
DE3532232A1 (de) * 1985-09-10 1987-03-19 Katec Betz Gmbh & Co Vorrichtung zum verbrennen oxidierbarer bestandteile in einem traegergas

Also Published As

Publication number Publication date
CA2037864A1 (fr) 1991-09-11
EP0447631A2 (fr) 1991-09-25
ATE102327T1 (de) 1994-03-15
DE59004810D1 (de) 1994-04-07
EP0447631A3 (en) 1992-03-11

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