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A method and an apparatus for gasifying combustible dusts in an entrained flow gasifier with several gasification burners. Each gasification burner is associated with one or a plurality of lock hopper and dosing systems having a plurality of supply flows. This has the advantage that the burners will

A method and an apparatus for gasifying combustible dusts in an entrained flow gasifier with several gasification burners. Each gasification burner is associated with one or a plurality of lock hopper and dosing systems having a plurality of supply flows. This has the advantage that the burners will continue to operate in the event of a failure of one supply flow.

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1. An apparatus for gasifying combustible dusts comprising hard coal, lignite, petroleum coke, or solid grindable residues, and slurries, comprising: an entrained gasification reactor for gasifying the combustible dusts at temperatures ranging from 1200 to 1900 C and pressures of up to 80 bar;wherei

1. An apparatus for gasifying combustible dusts comprising hard coal, lignite, petroleum coke, or solid grindable residues, and slurries, comprising: an entrained gasification reactor for gasifying the combustible dusts at temperatures ranging from 1200 to 1900 C and pressures of up to 80 bar;wherein said gasification reactor comprises a plurality of gasification burners, each burner having an individual feed port;wherein each gasification burner comprises a plurality of supply ports connected to said feed port;a plurality of lock hopper and dosing systems arranged to supply dust or slurries to the gasification burners; anda plurality of supply lines corresponding in number with said plurality of supply ports leading from each lock hopper and dosing system to said supply ports, and configured to provide dust or slurries to each feed port of every single burner. 2. The apparatus as set forth in claim 1, wherein a number of the plurality of lock hopper and dosing systems is fewer than the number of the plurality of gasification burners. 3. The apparatus as set forth in claim 2, wherein there are three gasification burners and two lock hopper and dosing systems. 4. The apparatus as set forth in claim 3, wherein each gasification burner is simultaneously supplied from two lock hopper and dosing systems through at least two supply lines, each of these two supply lines being associated with a different lock hopper and dosing system. 5. The apparatus as in claim 4, wherein said plurality of lock hopper and dosing systems are configured and arranged such that the burners will continue to operate steadily upon failure of one of them wherein each of said two lock hopper and dosing systems are coupled to each burner in a redundant manner so that redundancy is provided in the event of a system failure. 6. The apparatus as set forth in claim 1 wherein said plurality of lock hopper and dosing systems are configured to simultaneously supply dust or slurries to feed at least two of said plurality of gasification burners. 7. The apparatus as in claim 1, wherein, a plurality of the gasification burners are supplied uniformly with combustible dust. 8. The apparatus as in claim 1, wherein, all of the gasification burners are supplied uniformly with combustible dust. 9. The apparatus as in claim 1, wherein each of said plurality of gasification burners is coupled to said plurality of lock hopper and dosing systems such that said plurality of gasification burners are configured and arranged to prevent crooked burning in the gasification reactor. 10. The apparatus as in claim 1, further comprising at least one metering system coupled to said entrained gasification reactor. 11. The apparatus as in claim 10, wherein said at least one metering system comprises at least one bunker, at least two pressurized sluices, and at least one metering tank wherein an output of said metering system is coupled to said entrained gasification reactor. 12. A high capacity reactor for the gasification of pulverized fuel from solid fuels such as bituminous coals, lignite coals, and their cokes petroleum cokes, cokes from peat or biomass, in entrained flow, with an oxidizing medium containing free oxygen at temperatures between 1,200 and 1,900 degrees C. and at pressures between atmospheric pressure and 80 bar, into a crude synthesis gas and slag, the reactor comprising: a reactor head;an ignition and pilot burner disposed at said head of the reactor;a plurality of equal gasification burners disposed at said head of the reactor;a plurality of lock hoppers and dosing systems arranged to supply said pulverized fuels to said plurality of equal gasification burners;individual transport lines assigned to each gasification burner, said individual transport lines connecting and feeding said pulverized fuels from said lock hopper and dosing systems to the respective gasification burner;wherein every single gasification burner is connected and fed by at least two different lock hoppers and dosing systems; anda measuring system configured to measure and regulate amounts of pulverized fuel and oxygen flowing in each of said plurality of equal gasification burners, said measuring system controlling the overall total amounts of pulverized fuel and oxygen flowing in the reactor. 13. The high capacity reactor as in claim 12, wherein said plurality of equal gasification burners comprise at least three gasification burners and wherein said plurality of lock hoppers comprise at least three lock hoppers and dosing systems, wherein each gasification burner of said plurality of equal gasification burners is connected and fed with pulverized fuel over two burner individual transport lines with every single one of said three lock hoppers and dosing systems. 14. The high capacity reactor as in claim 12, wherein said plurality of equal gasification burners comprise three gasification burners and said plurality of lock hoppers and dosing systems comprise at least two lock hoppers and dosing systems, wherein each gasification burner is connected and fed with pulverized fuel over two burner individual transport lines with every single of said two lock hoppers and dosing systems. 15. The high capacity reactor as in claim 12, wherein said plurality of lock hopper and dosing systems are configured and arranged such that the burners will continue to operate steadily upon failure of one of them wherein each of said at least two lock hopper and dosing systems are coupled to each of said plurality of equal gasification burners in a redundant manner so that redundancy is provided in the event of a system failure. 16. The high capacity reactor as in claim 12, wherein a plurality of the gasification burners are supplied uniformly with combustible dust. 17. The high capacity reactor as in claim 12, wherein all of the gasification burners are supplied uniformly with combustible dust. 18. The high capacity reactor as in claim 12, wherein each of said plurality of gasification burners is coupled to said plurality of lock hopper and dosing systems such that said plurality of gasification burners are configured and arranged to prevent crooked burning in the gasification reactor. 19. The high capacity reactor as in claim 12, wherein said measuring system further comprises least one bunker, at least two pressurized sluices, and at least one metering tank wherein an output of said metering system is coupled to said entrained gasification reactor. 20. The high capacity reactor as in claim 19, further comprising at least one fluidizing gas line which leads into said at least one metering tank from below, and which provides for fluidizing the fuel.