[go: up one dir, main page]

DE1667324C3 - Tube fission furnace with reaction tubes provided with inner insulation at the lower end - Google Patents

Tube fission furnace with reaction tubes provided with inner insulation at the lower end

Info

Publication number
DE1667324C3
DE1667324C3 DE1667324A DE1667324A DE1667324C3 DE 1667324 C3 DE1667324 C3 DE 1667324C3 DE 1667324 A DE1667324 A DE 1667324A DE 1667324 A DE1667324 A DE 1667324A DE 1667324 C3 DE1667324 C3 DE 1667324C3
Authority
DE
Germany
Prior art keywords
reaction
tube
reaction tube
furnace
insulation
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
Application number
DE1667324A
Other languages
German (de)
Other versions
DE1667324B2 (en
DE1667324A1 (en
Inventor
Hans-Dieter Dipl.Ing. 4600 Dortmund Marsch
Paul Dipl.-Ing. 5841 Lichtendorf Mevenkamp
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.)
ThyssenKrupp Industrial Solutions AG
Original Assignee
Friedrich Uhde GmbH
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
Priority to FRJ8061696*8A priority Critical patent/FR96160E/fr
Priority claimed from DE19661542541 external-priority patent/DE1542541A1/en
Application filed by Friedrich Uhde GmbH filed Critical Friedrich Uhde GmbH
Priority to NL686816797A priority patent/NL140161B/en
Priority to ES360978A priority patent/ES360978A2/en
Priority to US780539A priority patent/US3600141A/en
Priority to JP43088390A priority patent/JPS5112644B1/ja
Priority to GB57608/68A priority patent/GB1244018A/en
Publication of DE1667324A1 publication Critical patent/DE1667324A1/en
Publication of DE1667324B2 publication Critical patent/DE1667324B2/en
Publication of DE1667324C3 publication Critical patent/DE1667324C3/en
Application granted granted Critical
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • B01J19/0073Sealings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • B01J8/062Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes being installed in a furnace
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/14Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
    • C10G9/18Apparatus
    • C10G9/20Tube furnaces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00074Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00081Tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/0015Controlling the temperature by thermal insulation means
    • B01J2219/00155Controlling the temperature by thermal insulation means using insulating materials or refractories
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00157Controlling the temperature by means of a burner
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Description

Hierzu 1 Blatt Zek -.α-.ngenFor this 1 sheet of Zek -.α-. nong

Claims (1)

1 21 2 Isolierung zwischen diesem Zcntralrohr und demIsolation between this Zcntralrohr and the Patentanspruch: Reaktionsrohr angeordnet ist. Um die KatalysatorClaim: Reaction tube is arranged. To the catalyst masse aus dem Reaktionsrohr nach unten abführenRemove the mass from the reaction tube downwards Röhrenspaitofen zur indirekten Erhitzung zu können, sind die Reaktionsrohre mit den Sammelvon spaltbaren Medien, insbesondere für die 5 leitungen über Flanschverbindungen verbunden.
Spaltung von Kohlenwasserstoffen zur Gewin- Soll oder kann die Katalysatormasse nach oben nung von Synthesegas, Stadtgas und Wasserstoff aus den Rohren abgesaugt werden, so ist es nicht errnit einer Mehrzahl von vertikalen Reaktionsroh- forderlich, zwischen den Reaktionsrohren und den ren und Sammelleitungen, wobei die Reaktions- Sammelleitungen Flanschverbindungen vorzusehen, rohre an ihrem unteren Ende mit den Sammellei- io Durch die Ausführung ohne Flanschverbindungen tungen verbunden sind und die Sammelleitungen zwischen den Reaktionsrohren und den Sammelleidie Reaktionsrohre tragen, die Sammelleitungen tungen werden zahlreiche Flanschenpaare eingespart unterhalb des Ofenbodens liegen, die Sammellei- und auch die Gefahr von Undichtigkeiten durch untungen eine Innenisolation aufweisen, die Reak- ter Wärmespannungen verzogene Flanschenpaare tionsrohre am unteren Ende mit einer Innenisola- 15 vermieden. Soll bei einer derartigen Ausführung ein tion versehen sind, die von der Anschlußstelle Reaktionsrohr zu Reparaturzwecken aus dem Ofen der Sammelleitungen bis etwa zur Oberkante des entfernt werden, so kann in diesem Fall, insbeson-Ofcnbodens reicht und sich innerhalb der Isola- dere bei Verwendung von Kohlenstoffstahl als Vertion jeweils ein Rohr zur Durchleitung des Reak- Jängerung des Reaktionsrohres bzw. aJs Übergangstionsgases befindet, nach Patent 1 542 530, d a - ao stück und der sich daraus ergebenden leichten durch gekennzeichnet, daß das inner- Brenn- und Schweißbarkeit, das Reaktionsroh auf halb der Isolation (27) des Reaktionsrohres (24) einfache Weise von der Sammelleitung abgetrennt befindliche Zentralrohr (26) bis in den Sammler werden und anschließend durch eine auf der Bau-(11) hineinragt und zwischen dem Zentralrohr stelle leicht auszuführende Schweißnaht wieder ein-(26) und dem Reaktionsrohr (24) in Höhe des 35 gesetzt werden.
To be able to use a tubular split furnace for indirect heating, the reaction tubes are connected to the collection of fissile media, especially for the 5 lines, via flange connections.
Splitting of hydrocarbons for profit or if the catalyst mass can be sucked upwards with synthesis gas, town gas and hydrogen from the pipes, it is not necessary to have a plurality of vertical reaction pipes between the reaction pipes and the pipes and manifolds, with the Reaction manifolds to provide flange connections, tubes at their lower end with the manifold. Due to the design without flange connections and the manifolds between the reaction tubes and the manifolds carry the reaction tubes, the manifolds will save numerous pairs of flanges below the furnace floor, the manifold - and also have the risk of leaks through the underside of an inner insulation, which avoids the reactor thermal stresses distorted flange pairs at the lower end with an inner insulation. If, in such an embodiment, a device is to be provided that is removed from the connection point of the reaction tube for repair purposes from the furnace of the collecting lines up to approximately the upper edge of the, then in this case, in particular, the furnace base can reach and be located within the insulation when using Carbon steel as vertion is a pipe for the passage of the reaction tube or aJs transition gas, according to patent 1 542 530, there - ao piece and the resulting light is characterized by the fact that the inner flammability and weldability, the reaction tube Halfway through the insulation (27) of the reaction tube (24), the central tube (26) is easily separated from the manifold and then extends into the collector and then protrudes through a weld seam on the construction (11) and between the central tube that is easy to make again - (26) and the reaction tube (24) at the height of 35.
Ofenbodens (21) ein Abdichtungsstück (32) an- Es wurde nun gefunden, daß bei ReaktionsrohrenIt has now been found that with reaction tubes geordnet ist, welches Reaktionsrohr und Zentral- mit einer Schweißverbindung zur Sammelleitung und rohr gasdicht miteinander verbindet. mit Innenisolierung im unteren Teil Kriechströme amis arranged, which reaction tube and central with a welded connection to the manifold and pipe connects to each other in a gastight manner. with inner insulation in the lower part, leakage currents on äußeren Kohlenstoffstahlteil vermieden werden kön-30 nen, wenn das innerhalb der Isolation des Reaktionsrohres befindliche Zentralrohr bis in den Sammler hineinragt und zwischen dem Zentralrohr und dem Reaktionsrohr in Höhe des Ofenbodens ein Abdichtungsstück angeordnet ist, weiches Reaktionsrohr 35 und Zentralrohr gasdicht miteinander verbindet.The outer carbon steel part can be avoided if the central tube located within the insulation of the reaction tube extends into the collector protrudes and a sealing piece between the central tube and the reaction tube at the level of the furnace bottom is arranged, soft reaction tube 35 and central tube connects to each other in a gas-tight manner. Durch die erfindungsgemäße Ausgestaltung des Die Erfindung betrifft eine Verbesserung eines Gegenstandes des Hauptpatents ist es nicht möglich,The invention relates to an improvement of an object of the main patent, it is not possible j Röhrenspaltofens zur indirekten Erhitzung von spalt- daß bei einer undichten Innenisolierung Reaktions-j Tube furnace for indirect heating of cracks that, in the event of a leaky inner insulation, reaction \ baren Medien, insbesondere für die Spaltung von gase in Form von Kriechströmen an die Wand des \ Cash media, especially for the cleavage of gases in the form of leakage to the wall of Kohlenwasserstoffen zur Gewinnung von Synthese- 40 Außenrohres bzw. Reaktionsrohres gelangen und dasHydrocarbons reach the production of synthesis 40 outer tube or reaction tube and that {>. gas, Stadtgas und Wasserstoff, mit einer Mehrzahl Außenrohr, welches aus Kohlenstoffstahl besteht, auf {>. gas, town gas and hydrogen, with a plurality of outer tubes made of carbon steel von vertikalen Reaktionsrohren und Sammelleitun- diese Weise unzulässig hoch erhitzt wird.vertical reaction tubes and manifolds - is heated to an unacceptably high level in this way. ι gen, wobei die Reaktionsrohre an ihrem unteren Die Zeichnung zeigt einen Schnitt durch den unte-ι gene, the reaction tubes at their lower The drawing shows a section through the lower Ende mit den Sammelleitungen verbunden sind, die ren Teil einer beispielhaften Ausführung des Reak-End are connected to the manifolds, the ren part of an exemplary embodiment of the reactor f Sammelleitungen die Reaktionsrohre tragen, die 45 tionsrohres in seiner Verbindung mit der Sammellei-f manifolds carry the reaction tubes, the 45 tion tube in its connection with the manifold Sammelleitungen unterhalb des Ofenbodens liegen, tung. Das Ende des Reaktionsrohres 24 ist an derCollecting lines are below the furnace floor, processing. The end of the reaction tube 24 is at the die Sammelleitungen eine Innenisolation aufweisen, Stelle, an der die erhöhten Rohrwandtemperaturenthe collecting lines have an inner insulation, point at which the increased pipe wall temperatures \ die Reaktionsrohre am unteren Ende mit einer Innen- infolge Wärmeableitung ab^-baut sind, durch eine \ the reaction tubes at the lower end with an internal as a result of heat dissipation are degraded by a fs isolation versehen sind, die von der Anschlußstelle Schweißnaht (30) mit dem Rohrstück 31, das ausfs insulation are provided, the weld seam from the connection point (30) with the pipe section 31, which is made of j§ der Sammelleitungen bis etwa zur Oberkante des 50 normalem Kohlenstoffstahl besteht, verbunden. Derj§ of the manifolds up to about the top of the 50 normal carbon steel is connected. Of the f. Ofenbodens reicht und sich innerhalb der Isolation unter dem Ofenboden 21 befindliche Teil des Reak- f. furnace bottom is enough and part of the reactor located within the insulation under the furnace bottom 21 jeweils ein Rohr zur Durchleitung des Reaktionsga- tionsrohres ist mit der Innenisolierung 27 versehen,one pipe for the passage of the reaction gas pipe is provided with the inner insulation 27, ses befindet, nach Patent 1 542 530. Durch die Innen- die sich zwischen dem Zentralrohr 26 und dem Ende isolation der Rohre wird erreicht, daß die Rohr- des Reaktionsrohres 24 befindet. Das Zentralrohr 26This is located, according to patent 1 542 530. By the inner which is located between the central tube 26 and the end Insulation of the tubes is achieved so that the tube of the reaction tube 24 is located. The central tube 26 !"' wandtemperatur unter dem Ofen schnell abgebaut 55 ist über das konische Abdichtungsstück 32 durchThe wall temperature under the furnace is quickly reduced 55 via the conical sealing piece 32 % wird. Dadurch wird es möglich, das unter dem Ofen eine Schweißnaht dicht mit dem Reaktionsrohr ver- % will. This makes it possible for a weld seam to be tightly sealed with the reaction tube under the furnace. befindliche Sammelleitungssystem aus normalem bunden. Über dem konischen Abdichtungsstück liegtlocated manifold system from normal bound. Lies over the conical sealing piece Kohlenstoffstahl auszuführen. Für den unteren Teil ein Katalysatorrost 33 auf. Der Katalysatorrost dientExecute carbon steel. A catalyst grate 33 for the lower part. The catalyst grate is used der Reaktionsrohre ist vorgesehen, das Reaktions- als Tragvorrichtung für die im Reaktionsrohr befindproduki durch ein Zentralrohr zu führen, wobei die 60 liehe Katalysatormasse.the reaction tube is provided, the reaction as a support device for the products located in the reaction tube to lead through a central tube, the 60 borrowed catalyst mass.
DE1667324A 1966-11-24 1967-12-04 Tube fission furnace with reaction tubes provided with inner insulation at the lower end Expired DE1667324C3 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
FRJ8061696*8A FR96160E (en) 1967-12-04
NL686816797A NL140161B (en) 1967-12-04 1968-11-25 TUBE OVEN.
ES360978A ES360978A2 (en) 1967-12-04 1968-12-02 Tube furnace for recovery of synthesis gases from hydrocarbon cracking
US780539A US3600141A (en) 1967-12-04 1968-12-02 Tube furnace for recovery of synthesis gases from hydrocarbon cracking
JP43088390A JPS5112644B1 (en) 1967-12-04 1968-12-04
GB57608/68A GB1244018A (en) 1967-12-04 1968-12-04 Improvements in tube furnaces for carrying out cracking processes

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19661542541 DE1542541A1 (en) 1966-11-24 1966-11-24 Reaction device with internal insulation
DEU0014469 1967-12-04

Publications (3)

Publication Number Publication Date
DE1667324A1 DE1667324A1 (en) 1971-06-16
DE1667324B2 DE1667324B2 (en) 1974-06-12
DE1667324C3 true DE1667324C3 (en) 1975-02-06

Family

ID=25752831

Family Applications (1)

Application Number Title Priority Date Filing Date
DE1667324A Expired DE1667324C3 (en) 1966-11-24 1967-12-04 Tube fission furnace with reaction tubes provided with inner insulation at the lower end

Country Status (1)

Country Link
DE (1) DE1667324C3 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3540782A1 (en) * 1985-11-16 1987-05-21 Uhde Gmbh Apparatus for endothermal catalytic cracking of hydrocarbons
DE102006022898B3 (en) * 2006-05-15 2007-09-27 Uhde Gmbh Manifold for tube splitters
DE102006052937A1 (en) 2006-11-08 2008-05-21 Uhde Gmbh Manifold for tube splitters
DE102007031678A1 (en) * 2007-07-06 2009-01-08 Thermo Fisher Scientific (Bremen) Gmbh Device with a connection of two capillaries
DE102012015667A1 (en) * 2012-08-09 2014-04-30 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Discharge system for a steam reformer and storage for this

Also Published As

Publication number Publication date
DE1667324B2 (en) 1974-06-12
DE1667324A1 (en) 1971-06-16

Similar Documents

Publication Publication Date Title
DE2008311C3 (en) Heat exchanger
DE1667324C3 (en) Tube fission furnace with reaction tubes provided with inner insulation at the lower end
DE3145292C2 (en) Tube fission furnace for indirect heating of fissile media
DE1542530C3 (en) Tube fission furnace
EP0242504A2 (en) Apparatus for the gasification of finely divided, particularly solid fuels under a high pressure
DE2829363A1 (en) Open fireplace that can be used as a hot water heater
DE2518836C2 (en) Submersible hot gas liquid heater
DE102009034870A1 (en) Gasification reactor for the production of CO or H2-containing raw gas
DE3245636A1 (en) Split-tube furnace with encased split tubes
DE2635210C2 (en) Steam generator
DE202015106170U1 (en) Residual flow reactor for the production of synthesis gas
DE3012596C2 (en)
DE1802505A1 (en) Process and arrangement for the conversion of hydrocarbons
DE3530715C2 (en)
DE2640728A1 (en) HEAT TRANSFER, PREFERRED FOR GAS MEDIA
DE2726459A1 (en) STEAM GENERATOR RISING ON THE GROUND
CN214287445U (en) Arrangement structure of acid gas removal equipment
DE1579985A1 (en) Heat exchanger downstream of a heating boiler
DE2540024B2 (en) SELF-SUPPORTING WATER PIPE STEAM GENERATOR
DE179939C (en)
DE2153965A1 (en) STEAM GENERATOR WITH FLAT COMBUSTION CHAMBER FLOOR
DE33242C (en) Steam boiler with lower boilers, which are connected by transverse boilers
DE1244729B (en) Industrial furnace
DE2729081A1 (en) EXHAUST BOILER SYSTEM
DE578743C (en) Water tube boiler for central heating systems

Legal Events

Date Code Title Description
C3 Grant after two publication steps (3rd publication)
E77 Valid patent as to the heymanns-index 1977
EGA New person/name/address of the applicant