WO1998045388A2 - Synthesis gas generator with combustion and quench chambers - Google Patents

Synthesis gas generator with combustion and quench chambers Download PDF

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Publication number
WO1998045388A2
WO1998045388A2 PCT/IB1998/000803 IB9800803W WO9845388A2 WO 1998045388 A2 WO1998045388 A2 WO 1998045388A2 IB 9800803 W IB9800803 W IB 9800803W WO 9845388 A2 WO9845388 A2 WO 9845388A2
Authority
WO
WIPO (PCT)
Prior art keywords
quench
combustion
chamber
gas generator
synthesis gas
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.)
Ceased
Application number
PCT/IB1998/000803
Other languages
French (fr)
Other versions
WO1998045388A3 (en
Inventor
Klaus Köhnen
Wolfgang Deeke
Jürgen HEERING
Wolfram Gruhlke
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.)
GEA Group AG
Original Assignee
Metallgesellschaft AG
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 Metallgesellschaft AG filed Critical Metallgesellschaft AG
Priority to AU72284/98A priority Critical patent/AU7228498A/en
Priority to AT98919418T priority patent/ATE204014T1/en
Priority to EP98919418A priority patent/EP0973847B1/en
Priority to DE69801317T priority patent/DE69801317T2/en
Publication of WO1998045388A2 publication Critical patent/WO1998045388A2/en
Publication of WO1998045388A3 publication Critical patent/WO1998045388A3/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/485Entrained flow gasifiers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/50Fuel charging devices
    • C10J3/506Fuel charging devices for entrained flow gasifiers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/82Gas withdrawal means
    • C10J3/84Gas withdrawal means with means for removing dust or tar from the gas
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/82Gas withdrawal means
    • C10J3/84Gas withdrawal means with means for removing dust or tar from the gas
    • C10J3/845Quench rings
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00Purifying combustible gases containing carbon monoxide
    • C10K1/08Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
    • C10K1/10Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
    • C10K1/101Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids with water only
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00Details of gasification apparatus
    • C10J2200/09Mechanical details of gasifiers not otherwise provided for, e.g. sealing means
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00Details of gasification apparatus
    • C10J2200/15Details of feeding means
    • C10J2200/152Nozzles or lances for introducing gas, liquids or suspensions
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/093Coal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/16Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1625Integration of gasification processes with another plant or parts within the plant with solids treatment
    • C10J2300/1628Ash post-treatment
    • C10J2300/1634Ash vitrification
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Definitions

  • the present invention pertains to a synthesis gas generator with combustion and quench chambers for generating, cooling and cleaning gases, which are generated by partial oxidation in the combustion chamber of a synthesis gas generator.
  • Such synthesis gas generators have been known in various design embodiments.
  • the partial oxidation of fuels e.g., coal, oil, sewage sludge, plastic wastes, natural gas, etc., with the aim of generating synthesis gas and utilizing it offers wide possibilities of application.
  • a waste heat utilization system or a quenching means is arranged downstream of the gas generated by partial oxidation.
  • a quenching medium e.g., water, is fed into the gas in the quenching means to cool it.
  • a synthesis gas generator is provided with combustion and quench chambers for generating, cooling and cleaning gases, which are generated by partial oxidation in the combustion chamber of a synthesis gas generator.
  • the cone extends into the water bath chamber gas space, forming a useful gas path whereby useful gas leaves the synthesis gas generator with the combustion chamber and the quench chamber, via the gas outlet pipes, after a 180° deflection around a rear- side area of the cone.
  • fuel and oxygen are introduced into the combustion chamber via burners, and a useful gas is generated by partial oxidation, and the useful gas is fed into the quenching zone of a quench chamber via a connection channel.
  • the useful gas is cooled at the inlet of the quench chamber by a nozzle system, which is arranged uniformly on the circumference, via which a quenching medium is sprayed in.
  • a nozzle system which is arranged uniformly on the circumference, via which a quenching medium is sprayed in.
  • one or more nozzle levels with nozzle assemblies may be arranged.
  • the temperature of the useful gas is lowered by means of the quenching medium sprayed in. After the quenching, the useful gas leaves the quench chamber via a cone at a high velocity, meets a water bath, and is then deflected by 180° and is sent to the gas outlet pipes.
  • the synthesis gas generator with combustion and quench chambers may be arranged as one unit in a common pressure vessel.
  • the combustion and quench chambers are designed as separate units and are connected to an overall unit by means of a flange connection.
  • the gas is generated by means of burners in the combustion chamber.
  • the cooling is ensured by a quenching medium, which is introduced into the quench chamber in a finely distributed form via the quenching nozzles of the nozzle assemblies.
  • the solids and liquid drops are removed due to the high velocity of the gas in the outlet cone, the impact on the water bath, and the subsequent deflection by 180° in the direction of the gas outlet openings.
  • Figure 1 is a longitudinal sectional view through the synthesis gas generator with integrated quenching means
  • Figure 2 is a longitudinal sectional view through the synthesis gas generator with separate quenching means
  • Figure 3 is a longitudinal sectional view through the quenching means with cooling basket.
  • Figure 4 is a sectional A-A according to Figure 3 with the arrangement of the nozzle assemblies with nozzles.
  • the useful gas and the molten slag leave the combustion chamber, flowing from top to bottom, and enter the quench chamber 7 at a high velocity via the connection channel (jet forming means) 6.
  • the nozzle assemblies 10, 11 may be arranged at different levels.
  • the nozzle assemblies are equipped with both a coolant connection 12 and a cold gas connection 13 (for, e.g., nitrogen). Both connections have shutoff fittings 14, 15 and flowmeters 16, 17 to ensure the uniform admission of the cooling medium into the quench chamber. If water is used as the cooling medium, nitrogen is used as a flushing and inertizing medium.
  • the nozzle assemblies 10, 11 are flanged to the pressurized jacket pipes 18, pass through the ceramic lining, and are installed in the cooling position in the quenching space of the quench chamber 7.
  • the cooling of the cone 20 by means of a cooling coil 28 is dispensable if a double-walled cone (not shown) with inner cooling (coolant flow channels in the double walled cone) is used.
  • the useful gas cooled in the quench chamber 7 leaves the quench chamber 7 via the tapering cone 20.
  • the useful gas carries solid particles and coolant drops, i.e., water drops, and is greatly accelerated in the cone 20 and is directed frontally to a water bath 21. Based on the high velocity and the relatively large mass of the solid and liquid coolant particles, they are unable to be deflected by 180° to the gas outlet pipes 23, but they impact on the surface of the water bath 21, are taken up by the water bath, and are thus separated from the gas flow.
  • the gas cleaned to remove the solids is deflected by 180° and it leaves the synthesis gas generator via the gas outlet pipes 23 after passing through a calming space 22.
  • the solids particles e.g., slag, which have fallen into the water bath, are separated via the solid outlet pipes 24.
  • Figure 2 shows the synthesis gas generator with separate quench chamber vessel.
  • the basic principles and the mode of operation are the same as those described in Figure 1. The only difference is that there are two separate pressure vessels 30, 31 for the combustion chamber 3 and the quench chamber 7 , and these pressure vessels are connected by means of a flange connection 33 to form one equipment unit.
  • Figure 3 shows a longitudinal section through a synthesis gas generator with integrated quenching means. The quench chamber 7 is provided with a cooling system here.
  • the cooling system comprises a cooling basket 41, a gas-tight welded construction consisting of cooling tubes and webs, which are provided with a ring distributor 43 and a ring collector 44.
  • Water feed lines 45 and water outlet lines 46 which are passed through the pressure vessel, are arranged at the ring distributor 43 and ring collector 44, respectively.
  • the fixed points 47 of the cooling system are also provided in this area, so that the cooling basket 41 has a possibility of expanding freely in the downward direction.
  • the nozzle assemblies 10, 11 are passed through the cooling basket 41 according to DE 195 33 908 Al which is incorporated herein by reference.
  • FIG. 4 section A-B according to Figure 3 shows the position of the nozzle assemblies 10, 11 in the quench chamber 7.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Industrial Gases (AREA)
  • Pre-Mixing And Non-Premixing Gas Burner (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

A synthesis gas generator with a combustion chamber and quench chamber for generating, cooling and cleaning gases, which are generated by partial oxidation in the combustion chamber of the synthesis gas generator. The combustion chamber (3) and the quench chamber (7) are separate chambers connected by a flow channel (6). Nozzle assemblies (10, 11) with nozzle heads (9, 34), which spray in a quenching medium (8), are arranged in the gas inlet area of the quench chamber (7). The quench zone within the quench chamber (7) is joined by a useful gas-quenching medium-mixing zone. A cone (20) is located at the outlet of the quench chamber. This cone is followed by a water bath (21). The useful gas leaves the synthesis gas generator after deflection by 180° in the rear-side area of the cone (20) via gas outlet openings (23).

Description

TITLE
SYNTHESIS GAS GENERATOR WITH COMBUSTION AND QUENCH CHAMBERS
FIELD OF THE INVENTION
The present invention pertains to a synthesis gas generator with combustion and quench chambers for generating, cooling and cleaning gases, which are generated by partial oxidation in the combustion chamber of a synthesis gas generator.
BACKGROUND OF THE INVENTION
Such synthesis gas generators have been known in various design embodiments. The partial oxidation of fuels, e.g., coal, oil, sewage sludge, plastic wastes, natural gas, etc., with the aim of generating synthesis gas and utilizing it offers wide possibilities of application.
Some of the possible applications are:
Generation of synthesis gas for gas and steam plants, generation of city gas, supplying chemical plants with synthesis gases, disposal of wastes (sewage sludge, plastics, residual distillates) with the generation of a high-value product gas (H2 and CO) , and generation of H2 for reduction in steel-making.
Depending on the needs of the application, a waste heat utilization system or a quenching means is arranged downstream of the gas generated by partial oxidation. A quenching medium, e.g., water, is fed into the gas in the quenching means to cool it.
SUMMARY AND OBJECTS OF THE INVENTION
The object of the present invention is to provide an especially advantageous device, in which useful gas is generated, cooled and cleaned by removing coarse, solid and liquid particles.
According to the invention, a synthesis gas generator is provided with combustion and quench chambers for generating, cooling and cleaning gases, which are generated by partial oxidation in the combustion chamber of a synthesis gas generator.
The generator includes a combustion chamber and a quench chamber separate from the combustion chamber. A connection channel is provided whereby the combustion chamber is connected to the quench chamber by the connection channel, a useful (product) gas stream flowing through the connection channel into the quench chamber. Nozzle assemblies are provided including quench nozzles which spray a quenching medium in a finely distributed form into the useful gas stream arranged in a gas inlet area of the quench chamber. A useful gas-quenching medium mixing zone is provided joining a quench zone within the quench chamber. A cone is arranged at an outlet of the quench chamber. A water bath region is provided with a gas space and a water space. Outlet pipes are provided extending into the generator. The cone extends into the water bath chamber gas space, forming a useful gas path whereby useful gas leaves the synthesis gas generator with the combustion chamber and the quench chamber, via the gas outlet pipes, after a 180° deflection around a rear- side area of the cone.
According to the present invention, fuel and oxygen are introduced into the combustion chamber via burners, and a useful gas is generated by partial oxidation, and the useful gas is fed into the quenching zone of a quench chamber via a connection channel. The useful gas is cooled at the inlet of the quench chamber by a nozzle system, which is arranged uniformly on the circumference, via which a quenching medium is sprayed in. Depending on the needs, one or more nozzle levels with nozzle assemblies may be arranged.
The temperature of the useful gas is lowered by means of the quenching medium sprayed in. After the quenching, the useful gas leaves the quench chamber via a cone at a high velocity, meets a water bath, and is then deflected by 180° and is sent to the gas outlet pipes.
Due to the high velocity and the great deflection after the cone, larger solid particles and drops of water are separated into the water bath. Thus, the gas leaves the synthesis gas generator cleaned and free from droplets.
The quench chamber may have uncooled or cooled chamber walls. The uncooled walls are lined with ceramic material, and the cooled walls consist of a water- cooled tube-web-tube wall.
The synthesis gas generator with combustion and quench chambers may be arranged as one unit in a common pressure vessel. In one alternative, the combustion and quench chambers are designed as separate units and are connected to an overall unit by means of a flange connection.
The gas is generated by means of burners in the combustion chamber. The cooling is ensured by a quenching medium, which is introduced into the quench chamber in a finely distributed form via the quenching nozzles of the nozzle assemblies. The solids and liquid drops are removed due to the high velocity of the gas in the outlet cone, the impact on the water bath, and the subsequent deflection by 180° in the direction of the gas outlet openings.
Exemplary embodiments of the present invention will be explained in greater detail on the basis of schematic drawings.
The various features of novelty which characterize the invention are pointed out with particularity in the claims annexed to and forming a part of this disclosure. For a better understanding of the invention, its operating advantages and specific objects attained by its uses, reference is made to the accompanying drawings and descriptive matter in which a preferred embodiment of the invention is illustrated. BRIEF DESCRIPTION OF THE DRAWINGS
In the drawings:
Figure 1 is a longitudinal sectional view through the synthesis gas generator with integrated quenching means;
Figure 2 is a longitudinal sectional view through the synthesis gas generator with separate quenching means;
Figure 3 is a longitudinal sectional view through the quenching means with cooling basket; and
Figure 4 is a sectional A-A according to Figure 3 with the arrangement of the nozzle assemblies with nozzles.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
As shown in Figure 1, fuel 1 enters a combustion chamber 3 via a burner 2. The fuel is gasified here, i.e., useful gas is generated. The combustion chamber 3 is lined with a ceramic material 4 in order to protect the pressurized jacket wall 5 of the combustion chamber 3 from excessively high temperatures. Based on the poor thermal conductivity of the ceramic material, nearly adiabatic gasification takes place. This has a favorable effect on the efficiency of the gasification.
The useful gas and the molten slag leave the combustion chamber, flowing from top to bottom, and enter the quench chamber 7 at a high velocity via the connection channel (jet forming means) 6. The cooling by a cooling medium 8, preferably water, which is introduced into the useful gas via the nozzle heads 9, 29 of the nozzle assemblies 10, 11, takes place in the quench chamber 7.
Depending on the needs, the nozzle assemblies 10, 11 may be arranged at different levels. The nozzle assemblies are equipped with both a coolant connection 12 and a cold gas connection 13 (for, e.g., nitrogen). Both connections have shutoff fittings 14, 15 and flowmeters 16, 17 to ensure the uniform admission of the cooling medium into the quench chamber. If water is used as the cooling medium, nitrogen is used as a flushing and inertizing medium.
The nozzle assemblies 10, 11 are flanged to the pressurized jacket pipes 18, pass through the ceramic lining, and are installed in the cooling position in the quenching space of the quench chamber 7.
Due to the arrangement of suitable passages 19 in the ceramic lining, it is possible to pull nozzle assemblies 10, 11 out of the quench space from the outside in the case of damage or for inspection.
This possibility of access eliminates the need for the time-consuming cooling of the synthesis gas generator and the expensive inspection or repair from the inside.
The cone 20 of the quench chamber 7 has a basic steel body, which is surrounded by a cooling coil 28 to which coolant is admitted. The dimensional stability of the cone 20 in relation to the hot chamber is guaranteed as a result, and it is, in addition, ensured that the ceramic lining of the basic conical steel body will not be damaged.
The cooling of the cone 20 by means of a cooling coil 28 is dispensable if a double-walled cone (not shown) with inner cooling (coolant flow channels in the double walled cone) is used.
The useful gas cooled in the quench chamber 7 leaves the quench chamber 7 via the tapering cone 20. The useful gas carries solid particles and coolant drops, i.e., water drops, and is greatly accelerated in the cone 20 and is directed frontally to a water bath 21. Based on the high velocity and the relatively large mass of the solid and liquid coolant particles, they are unable to be deflected by 180° to the gas outlet pipes 23, but they impact on the surface of the water bath 21, are taken up by the water bath, and are thus separated from the gas flow. The gas cleaned to remove the solids is deflected by 180° and it leaves the synthesis gas generator via the gas outlet pipes 23 after passing through a calming space 22.
The solids particles, e.g., slag, which have fallen into the water bath, are separated via the solid outlet pipes 24.
The inside of the pressure vessel 5, 31 is protected by a lining 27 against corrosion and excessive temperatures in the area in which it comes into contact with the useful gas.
Figure 2 shows the synthesis gas generator with separate quench chamber vessel. The basic principles and the mode of operation are the same as those described in Figure 1. The only difference is that there are two separate pressure vessels 30, 31 for the combustion chamber 3 and the quench chamber 7 , and these pressure vessels are connected by means of a flange connection 33 to form one equipment unit. Figure 3 shows a longitudinal section through a synthesis gas generator with integrated quenching means. The quench chamber 7 is provided with a cooling system here.
The cooling system comprises a cooling basket 41, a gas-tight welded construction consisting of cooling tubes and webs, which are provided with a ring distributor 43 and a ring collector 44. Water feed lines 45 and water outlet lines 46, which are passed through the pressure vessel, are arranged at the ring distributor 43 and ring collector 44, respectively. The fixed points 47 of the cooling system are also provided in this area, so that the cooling basket 41 has a possibility of expanding freely in the downward direction.
The nozzle assemblies 10, 11 are passed through the cooling basket 41 according to DE 195 33 908 Al which is incorporated herein by reference.
Figure 4 section A-B according to Figure 3 shows the position of the nozzle assemblies 10, 11 in the quench chamber 7.
While specific embodiments of the invention have been shown and described in detail to illustrate the application of the principles of the invention, it will be understood that the invention may be embodied otherwise without departing from such principles. APPENDIX
List of Reference Numbers
l. Fuel (fuel-oxygen mixture)
2. Burner
3. Combustion chamber . Ceramic material
5. Pressure jacket wall 6. Connection channel
7. Quench chamber
8. Cooling medium
9. Nozzle head
10. Nozzle assemblies 11. Nozzle assemblies
12. Cooling medium connection
13. Nitrogen connection
14. Shutoff fitting
15. Shutoff fitting 16. Flowmeter
17. Flowmeter
18. Pressure jacket pipe
19. Passages in (4)
20. Cone 21. Water bath
22. Calming space
23. Gas outlet pipe
2 . Solid outlet pipe
25. Inlet pipe cooling (10, 11) 26. Outlet pipe cooling (10, 11)
27. Lining in the area coming into contact with the useful gas)
28. Cooling coil (around 20)
29. Nozzle head 30. Pressure vessel (combustion chamber)
31. Pressure vessel (quench chamber)
33. Flange (between 30 and 31) 41. Cooling basket
42. Cone (of 41)
43. Ring distributor
4 . Ring collector
45. Water feed line
46. Water outlet line
47. Fixed point
48. Seal

Claims

WHAT IS CLAIMED IS:
1. A synthesis gas generator with combustion and quench chambers for generating, cooling and cleaning gases, which are generated by partial oxidation in the combustion chamber of a synthesis gas generator, the generator comprising: a combustion chamber; a quench chamber separate from said combustion chamber, a connection channel, said combustion chamber being connected to said quench chamber by said connection channel, a useful gas stream flowing through said connection channel into said quench chamber; nozzle assemblies including quench nozzles which spray a quenching medium in a finely distributed form into the useful gas stream arranged in a gas inlet area of said quench chamber; a useful gas-quenching medium mixing zone joining a quench zone within said quench chamber; a cone arranged at an outlet of said quench chamber; a water bath region with a gas space and a water space; outlet pipes, said cone extending into said water bath chamber gas space, forming a useful gas path whereby useful gas leaves the synthesis gas generator with said combustion chamber and said quench chamber, via said gas outlet pipes, after a 180° deflection around a rear-side area of said cone.
2. The synthesis gas generator with combustion and quench chambers in accordance with claim 1, wherein: said nozzle assemblies are arranged at an inlet of said quench chamber at different levels, and said nozzle assemblies at the different levels are offset in relation to one other circumferentially or are arranged flush.
3. The synthesis gas generator with combustion and quench chambers in accordance with claim 1, wherein said nozzle assemblies extend over different distances into said quench chamber.
4. The synthesis gas generator with combustion and quench chambers in accordance with claim l, wherein said nozzle assemblies are provided with interchangeable nozzle heads adapted to particular needs.
5. The synthesis gas generator with combustion and quench chambers in accordance with claim 1, wherein said combustion chamber and said quench chamber are lined with ceramic material.
6. The synthesis gas generator with combustion and quench chambers in accordance with claim l, wherein said combustion chamber is lined with ceramic material and said quench chamber is designed as a cooling basket form of cooling conduits.
7. The synthesis gas generator with combustion and quench chambers in accordance with claim 1, further comprising: penetration passages and seals said nozzle assemblies being inserted into said quench chamber from an outside and being sealed in an area of penetration of said passages.
8. The synthesis gas generator with combustion and quench chambers in accordance with claim 6, further comprising: a seals adjacent to a penetration passage of said cooling basket.
9. The synthesis gas generator with combustion and quench chambers in accordance with claim 1, wherein said combustion chamber and said quench chamber are either integrated in a common pressure vessel or are formed as separate units with separate vessels which are assembled into an overall unit by a flange connection.
10. The synthesis gas generator with combustion and quench chambers in accordance with claim 1, comprising: nozzle assemblies equipped with indirect cooling, which is fed via inlet and outlet pipes.
11. The synthesis gas generator with combustion and quench chambers in accordance with claim l, further comprising a lining inside of said pressure vessel in said useful gas contact area protecting said pressure vessel from corrosion and excessive temperature under a side of said quench chamber.
12. The synthesis gas generator with combustion and quench chambers in accordance with claim 1 wherein said nozzle assemblies are supplied with water via a said coolant connection with a shutoff fitting and a flowmeter and with a cold gas via a cold gas connection with a shutoff fitting and with a flowmeter 17.
13. The synthesis gas generator with combustion and quench chambers in accordance with claim 12 wherein said cold gas is nitrogen.
14. The synthesis gas generator with combustion and quench chambers in accordance with claim 1, wherein the said cone of said quench chamber has a basic steel body, around which a cooling coil is wound, and said cone is lined with ceramic on an inside.
15. Synthesis gas generator with combustion and quench chambers in accordance with claims 1, wherein said cone of said quench chamber is designed as a cooled double- walled construction, whose inside is lined with ceramic.
PCT/IB1998/000803 1997-04-08 1998-04-08 Synthesis gas generator with combustion and quench chambers Ceased WO1998045388A2 (en)

Priority Applications (4)

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AU72284/98A AU7228498A (en) 1997-04-08 1998-04-08 Synthesis gas generator with combustion and quench chambers
AT98919418T ATE204014T1 (en) 1997-04-08 1998-04-08 SYNTHEGASE GENERATOR WITH COMBUSTION AND QUENCHING CHAMBERS
EP98919418A EP0973847B1 (en) 1997-04-08 1998-04-08 Synthesis gas generator with combustion and quench chambers
DE69801317T DE69801317T2 (en) 1997-04-08 1998-04-08 SYNTHE GAS GENERATOR WITH COMBUSTION AND QUENCH CHAMBERS

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DE19714376.8 1997-04-08
DE19714376A DE19714376C1 (en) 1997-04-08 1997-04-08 Synthesis gas generator with combustion and quench chamber

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WO1998045388A2 true WO1998045388A2 (en) 1998-10-15
WO1998045388A3 WO1998045388A3 (en) 1999-01-07

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EP (2) EP0870818A3 (en)
JP (1) JPH10316976A (en)
KR (1) KR19980079750A (en)
AT (1) ATE204014T1 (en)
AU (1) AU7228498A (en)
DE (2) DE19714376C1 (en)
ES (1) ES2159952T3 (en)
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DE102007044726A1 (en) 2007-09-18 2009-03-19 Uhde Gmbh Synthesis gas producing method, involves drying and cooling synthesis gas in chamber, arranging water bath below another chamber, and extracting produced and cooled synthesis gas from pressure container below or lateral to latter chamber
WO2009036985A1 (en) 2007-09-18 2009-03-26 Uhde Gmbh Gasification reactor and method for entrained-flow gasification
US9290709B2 (en) 2007-09-18 2016-03-22 Thyssenkrupp Industrial Solutions Ag Gasification reactor and process for entrained-flow gasification
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CN102559275A (en) * 2012-03-13 2012-07-11 天津辰创环境工程科技有限责任公司 Water-cooling gasification furnace

Also Published As

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JPH10316976A (en) 1998-12-02
EP0973847A2 (en) 2000-01-26
AU7228498A (en) 1998-10-30
EP0973847B1 (en) 2001-08-08
US5976203A (en) 1999-11-02
ES2159952T3 (en) 2001-10-16
DE69801317T2 (en) 2001-11-22
WO1998045388A3 (en) 1999-01-07
ZA982765B (en) 1998-10-08
KR19980079750A (en) 1998-11-25
EP0870818A2 (en) 1998-10-14
EP0870818A3 (en) 1998-11-18
ATE204014T1 (en) 2001-08-15
DE19714376C1 (en) 1999-01-21
DE69801317D1 (en) 2001-09-13

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