EP2459683A2 - Gasification reactor for producing crude gas containing co or h2 - Google Patents

Gasification reactor for producing crude gas containing co or h2

Info

Publication number
EP2459683A2
EP2459683A2 EP10736620A EP10736620A EP2459683A2 EP 2459683 A2 EP2459683 A2 EP 2459683A2 EP 10736620 A EP10736620 A EP 10736620A EP 10736620 A EP10736620 A EP 10736620A EP 2459683 A2 EP2459683 A2 EP 2459683A2
Authority
EP
European Patent Office
Prior art keywords
wall
bulkheads
gasification reactor
drip edge
cylindrical wall
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
Application number
EP10736620A
Other languages
German (de)
French (fr)
Other versions
EP2459683B1 (en
Inventor
Eberhard Kuske
Johannes Dostal
Reinald Schulze Eckel
Lothar Semrau
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
ThyssenKrupp 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
Application filed by ThyssenKrupp Uhde GmbH filed Critical ThyssenKrupp Uhde GmbH
Priority to PL10736620T priority Critical patent/PL2459683T3/en
Publication of EP2459683A2 publication Critical patent/EP2459683A2/en
Application granted granted Critical
Publication of EP2459683B1 publication Critical patent/EP2459683B1/en
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C10J3/485—Entrained flow gasifiers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C10J3/485—Entrained flow gasifiers
    • C10J3/487—Swirling or cyclonic gasifiers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/74—Construction of shells or jackets
    • C10J3/76—Water jackets; Steam boiler-jackets
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/82—Gas withdrawal means
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/82—Gas withdrawal means
    • C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
    • C10J3/845—Quench rings
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/09—Mechanical details of gasifiers not otherwise provided for, e.g. sealing means

Definitions

  • the invention is directed to a gasification reactor for the production of CO- or H 2 -containing raw gas of the type specified in the preamble of claim 1.
  • Such a gasification reactor is known, for example, from WO 2009/036985 A1 of the Applicant, in which reference a wealth of further prior art is mentioned, such as US Pat. No. 4,474,584, which deals in particular with the cooling of the hot synthesis gas.
  • the invention is particularly concerned with problems encountered with such reactors, the invention not being limited to the gasification reactor specifically contemplated herein, and is also directed to apparatuses in which similar problems, as described in more detail below, may arise.
  • Such an apparatus must be suitable to allow methods of pressure gasification / combustion of finely divided fuels, including the partial oxidation of the fuels coal dust, finely divided biomass, oil, tars or the like. heard in a reactor.
  • This includes the separate or joint withdrawal of slag or fly ash and produced synthesis or flue gas.
  • Cooling of the reaction products must be made possible, for example by spray quenching, gas quenching, radiation quenching, convection heating surfaces or the like, depending on the type of process used, and finally attention is paid to the discharge of the reaction products must be directed from the pressure vessel.
  • a swirl flow is generated in order to be able to completely convert even coarser particles as well as to protect critical areas of the heating surfaces from too high a heat flow density. This is achieved by a burner setting of 1 to 20 ° in the horizontal plane.
  • the swirl generated must be removed from the flow again after leaving the reactor, so that the hot, sticky slag particles are not thrown against the pressure vessel protecting, unprotected heating surfaces and there to cause caking or damage.
  • the object of the invention is to provide a solution with which on the one hand a striation of the running ash can be achieved and on the other hand, the provision of another Schlackenabtropfkante, which ensures an optimal slag process.
  • this object is achieved according to the invention in that the bulkhead carrying the wall passes below the bulkheads via a shoulder with a wavy surface in a reduced diameter cylinder wall.
  • adjustability refers to an optimum setting with respect to the drip edge according to the given and operational requirements. After optimization, there is no need for further adjustability, especially not during operation of the reactor.
  • the invention also provides that the cylindrical second drip edge is surrounded by a diameter wall which is enlarged in diameter and which encloses at least part of a gas transition region. In practice, this outer cylindrical wall limits the transition region into the quench chamber or quench channel.
  • the invention also provides that at least one bulkhead of the fluidized-bed brake is equipped with a device for measuring the heat flux density.
  • the invention also provides that the second cylindrical wall and the further cylindrical wall are provided with a smooth, flat, corrosion-resistant surface, e.g. by using plated Super- ⁇ -tubes, wherein the swirl-reducing bulkheads, the undulating transitional surface and the cylinder wall providing the first drip-edge are formed as a standard pipe-web pipe wall with potting and potting.
  • FIG. 2 is a schematic sectional view of half of the gasification reactor in the transition region from the reaction space to the transition into the quench space (not shown) and in FIG
  • Fig. 3 shows the development of the transitional channel with swirl brakes forming reactor area.
  • the gasification reactor shown in FIG. 1, generally designated 1, has a pressure vessel 2 in which a reaction space 4 enclosed by a membrane wall 3 is arranged at a distance from the pressure vessel 2 from top to bottom.
  • the membrane inlet 3 acting on the coolant supply line is denoted by 5.
  • the membrane wall 3 passes via a lower cone 6 in a narrowed channel as part of a transition region designated 8, wherein in the narrowed transition channel 7 swirl brakes 9 are indicated.
  • 10a drip edge in the transition region 8 for the liquid ash in the transition region at a distance from the first drip edge 10 at the end of the transition channel 7 is designated.
  • the transition region 8 is followed by a quench chamber or quench channel 11, followed by a slag collecting container 12 in a water bath 13.
  • the wall 14 equipped with the swirl brakes 9 passes into a shoulder 15 which has a corrugated surface which is indicated in FIG. 3, the individual shafts being designated 16 are. This is followed by a smooth, in the Diameter changed cylinder wall 17, which provides a first drip edge 18.
  • the transitional channel 7 including the used for forming stratification of the slag configurations of the transition region between the wall 19 and the wall 18 is surrounded by a further, cylindrical wall which has an obliquely shown in Fig. 2 wall plate 20 with the transitional space 8 enclosing the cylindrical wall 21st connected in a gastight manner.
  • the cylindrical wall 19 enclosing the transition channel 7 provides the further, second drip edge designated by 10.
  • the system of cylindrical wall 19 and wall plate 20 in height or adjustable, which is indicated by a double arrow 22.
  • the such a adjustability enabling sealing areas or transition areas of the corresponding, with coolant flowing pipes are indicated in Fig. 2 only in principle and designated 23 and 24.
  • Fig. 2 is only symbolically indicated that at least one bulkhead 9 of the fluidized bed brake can be equipped with a device 25 for heat flow measurement.
  • the described embodiment of the invention is still to be modified in many ways, without departing from the spirit.
  • the waves 16 shown in an angled section according to FIG. 3 can be angular or curved in the corresponding wall ledge, depending on the application, the piping of the corresponding wall regions may be different. like. more.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Industrial Gases (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

The invention relates to a gasification reactor for producing crude gas containing CO or H2 by gasification of ash-containing fuel with oxygen-containing gas at temperatures above the fusion temperature of the ash, wherein a reaction chamber, formed by a membrane wall that is flown through by a cooling medium, is provided inside a pressure vessel, comprising a transition channel that is tapering into a gas cooling chamber. According to the invention, spin-reducing, cooled bulkheads are provided in the transition channel. The aim of the invention is, on the one hand, to achieve a strain formation of the draining ash and, on the other hand, to provide another slag drip edge that ensures an optimal slag drain. Said aim is achieved by the provision that the wall (14) supporting the bulkheads (9) changes below the bulkheads into a cylinder wall (17) having a reduced diameter via an step (21) with a corrugated surface, that the cylinder wall (17) having a reduced diameter is surrounded by another cylindrical wall (19) having a larger diameter, which forms on its end and in the direction of gravity a second slag drip edge (10) and that the additional cylindrical wall (19) is adjustably (arrow 22) arranged in its vertical position with respect to the first drip edge (18).

Description

"Vergasungsreaktor zur Herstellung von CO- oder H2- haltigem Rohgas" "Gasification reactor for the production of CO or H 2 -containing raw gas"
Die Erfindung richtet sich auf einen Vergasungsreaktor zur Herstellung von CO- oder H2-haltigem Rohgas der im Oberbegriff des Anspruches 1 angegebenen Gattung. The invention is directed to a gasification reactor for the production of CO- or H 2 -containing raw gas of the type specified in the preamble of claim 1.
Ein derartiger Vergasungsreaktor ist beispielsweise aus der WO 2009/036985 Al der Anmelderin bekannt, wobei in dieser Literaturstelle eine Fülle von weiterem Stand der Technik genannt ist, wie beispielsweise die US 4 474 584, die insbesondere die Kühlung des heißen Synthesegases behandelt. Such a gasification reactor is known, for example, from WO 2009/036985 A1 of the Applicant, in which reference a wealth of further prior art is mentioned, such as US Pat. No. 4,474,584, which deals in particular with the cooling of the hot synthesis gas.
Die Erfindung beschäftigt sich insbesondere mit Problemen, die bei derartigen Reaktoren auftauchen, wobei die Erfindung nicht auf den speziell hier angesprochenen Vergasungsreaktor beschränkt ist, sie richtet sich auch auf Apparate, bei denen ähnliche, weiter unten näher beschriebene Probleme auftauchen können. The invention is particularly concerned with problems encountered with such reactors, the invention not being limited to the gasification reactor specifically contemplated herein, and is also directed to apparatuses in which similar problems, as described in more detail below, may arise.
Ein derartiger Apparat muss geeignet sein, um Verfahren der Druckvergasung/Verbrennung von fein verteilten Brennstoffen zu ermöglichen, wozu die partielle Oxidation der Brennstoffe Kohlenstaub, fein verteilte Biomasse, Öl, Teere od. dgl . in einem Reaktor gehört . Hierzu gehört auch der getrennte oder gemeinsame Abzug von Schlacke oder Flugasche und erzeugtem Synthese- bzw. Rauchgas. Es muss eine Kühlung der Reaktionsprodukte (Gas und Schlacke/Flugasche) möglich gemacht werden, etwa durch Sprühquenchen, Gasquenchen, Strahlungs- quenchen, Konvektionsheizflachen od. dgl., je nach Art des eingesetzten Verfahrens, wobei schließlich auch ein Augenmerk auf die Ausschleusung der Reaktionsprodukte aus dem Druckbehälter gerichtet werden muss . In der oben genannten WO 2009/036985 Al wird eine Drallströmung erzeugt, um auch gröbere Partikel vollständig umsetzen zu können sowie kritische Bereiche der Heizflächen vor zu hoher Wärmestromdichte zu bewahren. Dies wird durch eine Brenneranstellung von 1 bis 20° in der Horizontalebene verwirklicht. Der erzeugte Drall muss nach Verlassen des Reaktors wieder aus der Strömung entfernt werden, damit die heißen, klebrigen Schlackepartikel nicht gegen die den Druckbehälter schützenden, ungeschützten Heizflächen geschleudert werden und dort Anbackungen oder Schäden zu verursachen. Such an apparatus must be suitable to allow methods of pressure gasification / combustion of finely divided fuels, including the partial oxidation of the fuels coal dust, finely divided biomass, oil, tars or the like. heard in a reactor. This includes the separate or joint withdrawal of slag or fly ash and produced synthesis or flue gas. Cooling of the reaction products (gas and slag / fly ash) must be made possible, for example by spray quenching, gas quenching, radiation quenching, convection heating surfaces or the like, depending on the type of process used, and finally attention is paid to the discharge of the reaction products must be directed from the pressure vessel. In the abovementioned WO 2009/036985 A1, a swirl flow is generated in order to be able to completely convert even coarser particles as well as to protect critical areas of the heating surfaces from too high a heat flow density. This is achieved by a burner setting of 1 to 20 ° in the horizontal plane. The swirl generated must be removed from the flow again after leaving the reactor, so that the hot, sticky slag particles are not thrown against the pressure vessel protecting, unprotected heating surfaces and there to cause caking or damage.
Entsprechende Drallbremsen sind beispielsweise in der DE 10 2009 005 464.2 beschrieben. Corresponding swirl brakes are described for example in DE 10 2009 005 464.2.
Aufgabe der Erfindung ist die Schaffung einer Lösung, mit der zum einen eine Strähnenbildung der ablaufenden Asche erreicht werden kann und zum anderen die Bereitstellung einer weiteren Schlackenabtropfkante, die für einen optimalen Schlackeablauf sorgt . The object of the invention is to provide a solution with which on the one hand a striation of the running ash can be achieved and on the other hand, the provision of another Schlackenabtropfkante, which ensures an optimal slag process.
Mit einem Vergasungsreaktor der eingangs bezeichneten Art wird diese Aufgabe gemäß der Erfindung dadurch gelöst, dass die die Schotten tragende Wand unterhalb der Schotten über einen Absatz mit gewellter Oberfläche in eine im Durchmesser verringerte Zylinderwand übergeht. With a gasification reactor of the type described, this object is achieved according to the invention in that the bulkhead carrying the wall passes below the bulkheads via a shoulder with a wavy surface in a reduced diameter cylinder wall.
Durch die gewellte Oberfläche und Tiefpunkte unterhalb der Schotten wird erreicht, dass die Schlacke gezielt in Strähnen aus den Wellentälern ablaufen kann und damit kein geschlossener Schlackefilm gebildet wird. Due to the undulating surface and the low points below the bulkheads, it is achieved that the slag can run off in targeted strands from the troughs and thus no closed slag film is formed.
Zusätzlich ist vorgesehen, dass die im Durchmesser verringerte Zylinderwand von einer im Durchmesser vergrößerten weiteren zylindrischen Wand umgeben ist, die in Schwerkraftrichtung an ihrem Ende eine zweite Schlackeabtropfkante bildet, wobei insbesondere vorgesehen ist, dass die weitere zylindrische Wand in ihrer vertikalen Position bezogen auf die erste Abtropfkante verstellbar angeordnet ist. In addition, it is provided that the reduced diameter in the cylinder wall of an enlarged diameter in another surrounded cylindrical wall which forms in the direction of gravity at its end a second Schlackeabtropfkante, wherein it is provided in particular that the further cylindrical wall is arranged adjustable in its vertical position relative to the first drip edge.
Ist hier von "Verstellbarkeit" die Rede, so betrifft diese eine optimale Einstellung gegenüber der Abtropfkante nach den gegebenen und betriebsbedingten Vorgaben. Nach Optimierung bedarf es einer weiteren Verstellbarkeit nicht, insbesondere nicht während des Betriebes des Reaktors . If the term "adjustability" is mentioned here, this refers to an optimum setting with respect to the drip edge according to the given and operational requirements. After optimization, there is no need for further adjustability, especially not during operation of the reactor.
Die Erfindung sieht auch vor, dass die zylindrische zweite Abtropfkante von einer im Durchmesser vergrößerten weiteren zylindrischen Wand umgeben ist, die wenigstens einen Teil eines Gasübergangsbereiches umschließt. In der Praxis begrenzt diese äußere zylindrische Wand den Übergangsbereich in den Quenchraum bzw. Quenchkanal . The invention also provides that the cylindrical second drip edge is surrounded by a diameter wall which is enlarged in diameter and which encloses at least part of a gas transition region. In practice, this outer cylindrical wall limits the transition region into the quench chamber or quench channel.
Die Erfindung sieht darüber hinaus auch vor, dass wenigstens ein Schott der Wirbelbremse mit einer Einrichtung zur Wärmestromdichte-Messung ausgerüstet ist. In addition, the invention also provides that at least one bulkhead of the fluidized-bed brake is equipped with a device for measuring the heat flux density.
In einer möglichen Ausgestaltung sieht die Erfindung auch vor, dass die zweite zylindrische Wand und die weitere zylindrische Wand mit einer glatten, ebenen, korrosionsbeständigen Oberfläche versehen sind, z.B. durch Verwendung von plattierten Super-Ω-Rohren, wobei die drallvermindernden Schotten, die wellenförmige Übergangsfläche und die die erste Abtropfkante bereitstellende Zylinderwand als Standard-Rohr-Steg-Rohrwand mit Bestiftung und Bestampfung ausgebildet ist. In one possible embodiment, the invention also provides that the second cylindrical wall and the further cylindrical wall are provided with a smooth, flat, corrosion-resistant surface, e.g. by using plated Super-Ω-tubes, wherein the swirl-reducing bulkheads, the undulating transitional surface and the cylinder wall providing the first drip-edge are formed as a standard pipe-web pipe wall with potting and potting.
Weitere Einzelheiten, Merkmale und Vorteile der Erfindung ergeben sich aufgrund der nachfolgenden Beschreibung sowie anhand der Zeichnung. Diese zeigt in Fig. 1 eine prinzipielle Schnittzeichnung durch einen erfindungsgemäßen Vergasungsreaktor, Further details, features and advantages of the invention will become apparent from the following description and from the drawing. This shows in 1 is a schematic sectional view through a gasification reactor according to the invention,
Fig. 2 eine Prinzipschnittzeichnung der Hälfte des Vergasungsreaktors im Übergangsbereich vom Reaktionsraum zum Übergang in den nicht näher dargestellten Quench- raum sowie in 2 is a schematic sectional view of half of the gasification reactor in the transition region from the reaction space to the transition into the quench space (not shown) and in FIG
Fig. 3 die Abwicklung des den Übergangskanal mit Drallbremsen bildenden Reaktorbereiches. Fig. 3 shows the development of the transitional channel with swirl brakes forming reactor area.
Der in Fig. 1 dargestellte, allgemein mit 1 bezeichnete Vergasungsreaktor weist einen Druckbehälter 2 auf, in dem von oben nach unten ein durch eine Membranwand 3 umschlossener Reaktionsraum 4 auf Abstand zum Druckbehälter 2 angeordnet ist. Die die Membranwand 3 beaufschlagende Kühlmittelzuleitung ist mit 5 bezeichnet. Dabei geht die Membranwand 3 über einen unteren Konus 6 in einen verengten Kanal als Teil eines mit 8 bezeichneten Übergangsbereiches über, wobei im verengten Übergangskanal 7 Drallbremsen 9 angedeutet sind. Mit 10a ist eine Abtropfkante im Übergangsbereich 8 für die flüssige Asche im Übergangsbereich im Abstand zur ersten Abtropfkante 10 am Ende des Übergangskanales 7 bezeichnet. The gasification reactor shown in FIG. 1, generally designated 1, has a pressure vessel 2 in which a reaction space 4 enclosed by a membrane wall 3 is arranged at a distance from the pressure vessel 2 from top to bottom. The membrane inlet 3 acting on the coolant supply line is denoted by 5. In this case, the membrane wall 3 passes via a lower cone 6 in a narrowed channel as part of a transition region designated 8, wherein in the narrowed transition channel 7 swirl brakes 9 are indicated. 10a, a drip edge in the transition region 8 for the liquid ash in the transition region at a distance from the first drip edge 10 at the end of the transition channel 7 is designated.
An den Übergangsbereich 8 schließt sich ein Quenchraum bzw. Quenchkanal 11, gefolgt von einem Schlackesammelbehälter 12 in einem Wasserbad 13 an. The transition region 8 is followed by a quench chamber or quench channel 11, followed by a slag collecting container 12 in a water bath 13.
Wie sich aus den Fig. 2 und 3 ergibt, geht die mit den die Drallbremse bildenden Schotten 9 ausgerüstete Wand 14 in einen Absatz 15 über, der eine gewellte Oberfläche aufweist, die in Fig. 3 angedeutet ist, wobei die einzelnen Wellen mit 16 bezeichnet sind. Hieran schließt sich wiederum eine glatte, im Durchmesser veränderte Zylinderwand 17 an, die eine erste Abtropfkante 18 bereitstellt. As can be seen from FIGS. 2 and 3, the wall 14 equipped with the swirl brakes 9 passes into a shoulder 15 which has a corrugated surface which is indicated in FIG. 3, the individual shafts being designated 16 are. This is followed by a smooth, in the Diameter changed cylinder wall 17, which provides a first drip edge 18.
Der Übergangskanal 7 einschließlich der zur Strähnenbildung der Schlacke herangezogenen Gestaltungen des Übergangsbereiches zwischen der Wand 19 und der Wand 18 ist von einer weiteren, zylindrischen Wand umgeben, die über eine in Fig. 2 schräg dargestellte Wandscheibe 20 mit der den Übergangsraum 8 umschließenden zylindrischen Wand 21 gasdicht in Verbindung steht. The transitional channel 7 including the used for forming stratification of the slag configurations of the transition region between the wall 19 and the wall 18 is surrounded by a further, cylindrical wall which has an obliquely shown in Fig. 2 wall plate 20 with the transitional space 8 enclosing the cylindrical wall 21st connected in a gastight manner.
Die Besonderheit liegt zum einen darin, dass die den Übergangskanal 7 umschließende zylindrische Wand 19 die weitere, mit 10 bezeichnete zweite Abtropfkante bereitstellt. Auch ist erfindungsgemäß das System aus zylindrischer Wand 19 und Wandscheibe 20 in der Höhe ein- bzw. verstellbar, was mit einem Doppelpfeil 22 angedeutet ist. Die eine derartige Einstellbarkeit ermöglichenden Dichtbereiche bzw. Übergangsbereiche der entsprechenden, mit Kühlmittel durchflossenen Rohre sind in Fig. 2 lediglich prinzipiell angedeutet und mit 23 und 24 bezeichnet . The peculiarity is, on the one hand, that the cylindrical wall 19 enclosing the transition channel 7 provides the further, second drip edge designated by 10. Also, according to the invention, the system of cylindrical wall 19 and wall plate 20 in height or adjustable, which is indicated by a double arrow 22. The such a adjustability enabling sealing areas or transition areas of the corresponding, with coolant flowing pipes are indicated in Fig. 2 only in principle and designated 23 and 24.
In Fig. 2 ist lediglich symbolisch angedeutet, dass wenigstens ein Schott 9 der Wirbelbremse mit einer Einrichtung 25 zur Wärmestrommessung ausgerüstet sein kann. In Fig. 2 is only symbolically indicated that at least one bulkhead 9 of the fluidized bed brake can be equipped with a device 25 for heat flow measurement.
Natürlich ist das beschriebene Ausführungsbeispiel der Erfindung noch in vielfacher Hinsicht abzuändern, ohne den Grundgedanken zu verlassen. So können die in Abwinkelung gemäß Fig. 3 dargestellten Wellen 16 im entsprechenden Wandabsatz eckig oder gekrümmt ausgebildet sein, je nach Einsatz kann die Verrohrung der entsprechenden Wandbereiche unterschiedlich sein u. dgl . mehr. Of course, the described embodiment of the invention is still to be modified in many ways, without departing from the spirit. Thus, the waves 16 shown in an angled section according to FIG. 3 can be angular or curved in the corresponding wall ledge, depending on the application, the piping of the corresponding wall regions may be different. like. more.

Claims

Patentansprüche : Claims:
1. Vergasungsreaktor zur Herstellung von CO- oder H2-haltigem Rohgas durch Vergasung von aschehaltigem Brennstoff mit sauerstoffhaltigem Gas bei Temperaturen oberhalb der 1. Gasification reactor for the production of CO- or H 2 -containing raw gas by gasification of ash-containing fuel with oxygen-containing gas at temperatures above the
Schmelztemperatur der Asche, wobei innerhalb eines Druckbehälters ein von einer kühlmediumdurchflossenen Membranwand gebildeter Reaktionsraum vorgesehen ist mit einem sich verjüngenden Übergangskanal in einen Gasabkühlraum, wobei im Übergangskanal drallvermindernde, gekühlte Schotten vorgesehen sind,  Melting temperature of the ash, wherein within a pressure vessel formed by a cooling medium-flowed membrane wall reaction space is provided with a tapered transition channel into a gas cooling chamber, wherein in the transition channel swirl reducing, cooled bulkheads are provided,
dadurch gekennzeichnet,  characterized,
- dass die die Schotten (9) tragende Wand (14) unterhalb der Schotten über einen Absatz (21) mit gewellter Oberfläche in eine im Durchmesser verringerte Zylinderwand (17) übergeht, - that the wall (14) carrying the bulkheads (14) passes beneath the bulkheads via a shoulder (21) with a corrugated surface into a cylinder wall (17) reduced in diameter,
- dass die im Durchmesser verringerte Zylinderwand (17) von einer im Durchmesser vergrößerten weiteren zylindrischen Wand (19) umgeben ist, die in Schwerkraftrichtung an ihrem Ende eine zweite Schlackeabtropfkante (10) bildet und- That the reduced diameter cylinder wall (17) is surrounded by an enlarged diameter in another cylindrical wall (19) which forms in the direction of gravity at its end a second Schlackeabtropfkante (10) and
- dass die weitere zylindrische Wand (19) in ihrer vertikalen Position bezogen auf die erste Abtropfkante (18) verstellbar (Pfeil 22) angeordnet ist. - That the further cylindrical wall (19) in its vertical position with respect to the first drip edge (18) adjustable (arrow 22) is arranged.
2. Vergasungsreaktor nach Anspruch 1, 2. Gasification reactor according to claim 1,
dadurch gekennzeichnet,  characterized,
dass die zylindrische zweite Abtropfkante (10) von einer im Durchmesser vergrößerten weiteren zylindrischen Wand (21) umgeben ist, die wenigstens einen Teil eines Gasübergangs- bereiches (8) umschließt.  in that the cylindrical second drip edge (10) is surrounded by a further cylindrical wall (21) which is enlarged in diameter and which encloses at least part of a gas transition area (8).
3. Vergasungsreaktor nach Anspruch 1 oder 2 , 3. Gasification reactor according to claim 1 or 2,
dadurch gekennzeichnet,  characterized,
dass wenigstens ein Schott (9) der Wirbelbremse mit einer Einrichtung zur Wärmestromdichte-Messung ausgerüstet ist. in that at least one bulkhead (9) of the fluidized-bed brake is equipped with a device for heat flow density measurement.
4. Vergasungsreaktor nach einem der vorangehenden Ansprüche, dadurch gekennzeichnet, 4. Gasification reactor according to one of the preceding claims, characterized in that
dass die zweite zylindrische Wand (19) und die weitere zylindrische Wand (21) mit einer glatten, ebenen, korrosionsbeständigen Oberfläche versehen sind, z.B. durch Verwendung von plattierten Super-Ω-Rohren, wobei die drallvermindernden Schotten (9) , die wellenförmige Übergangsfläche (16) und die die erste Abtropfkante (10) bereitstellende Zylinderwand (18) als Standard-Rohr-Steg-Rohrwand mit Bestiftung und Bestampfung ausgebildet ist.  the second cylindrical wall (19) and the further cylindrical wall (21) are provided with a smooth, flat, corrosion-resistant surface, e.g. by using clad Super Ω tubes, the swirl reducing bulkheads (9), the wavy transitional surface (16), and the cylinder wall (18) providing the first drip edge (10) are formed as a standard pipe-web pipe wall with potting and potting is.
EP10736620.5A 2009-07-27 2010-07-16 Gasification reactor for producing crude gas containing co or h2 Not-in-force EP2459683B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL10736620T PL2459683T3 (en) 2009-07-27 2010-07-16 Gasification reactor for producing crude gas containing co or h2

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102009034870A DE102009034870A1 (en) 2009-07-27 2009-07-27 Gasification reactor for the production of CO or H2-containing raw gas
PCT/EP2010/004337 WO2011012229A2 (en) 2009-07-27 2010-07-16 Gasification reactor for producing crude gas containing co or h2

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EP2459683A2 true EP2459683A2 (en) 2012-06-06
EP2459683B1 EP2459683B1 (en) 2015-03-18

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EP (1) EP2459683B1 (en)
KR (1) KR101636676B1 (en)
CN (1) CN102471708B (en)
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BR (1) BR112012001972B1 (en)
CA (1) CA2768592C (en)
DE (1) DE102009034870A1 (en)
ES (1) ES2539724T3 (en)
HK (1) HK1167676A1 (en)
PL (1) PL2459683T3 (en)
RU (1) RU2536983C2 (en)
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UA (1) UA103254C2 (en)
WO (1) WO2011012229A2 (en)
ZA (1) ZA201201353B (en)

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WO2021084016A1 (en) 2019-10-29 2021-05-06 Michiel Cramwinckel Process for a plastic product conversion

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ES2539724T3 (en) 2015-07-03
CN102471708A (en) 2012-05-23
EP2459683B1 (en) 2015-03-18
AU2010278406B2 (en) 2014-10-02
RU2536983C2 (en) 2014-12-27
BR112012001972A2 (en) 2016-03-08
WO2011012229A3 (en) 2011-06-30
TWI440708B (en) 2014-06-11
UA103254C2 (en) 2013-09-25
KR101636676B1 (en) 2016-07-07
PL2459683T3 (en) 2015-10-30
KR20120032006A (en) 2012-04-04
US20120189499A1 (en) 2012-07-26
RU2012106881A (en) 2013-09-10
DE102009034870A1 (en) 2011-02-03
CN102471708B (en) 2014-06-25
WO2011012229A2 (en) 2011-02-03
CA2768592A1 (en) 2011-02-03
US9045704B2 (en) 2015-06-02
BR112012001972B1 (en) 2018-02-06
ZA201201353B (en) 2012-11-28
HK1167676A1 (en) 2012-12-07
TW201109430A (en) 2011-03-16
AU2010278406A1 (en) 2012-02-02
CA2768592C (en) 2017-11-28

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