Method and device for starting up gasifying reactors operated with combustible dust

Patent metadata

Field	Value
Publication number	US-9670428-B2
Application number	US-200913056337-A
Country	US
Kind code	B2
Filing date	Jul 15, 2009
Priority date	Aug 1, 2008
Publication date	Jun 6, 2017
Grant date	Jun 6, 2017

Abstract

The invention relates to a method for starting up a gasifying reactor comprising a plurality of burners. Each burner is thereby charged with combustible dust from a metering vessel ( 1 ) via a dense flow conveyor line ( 51, 52, 53, 54 ), which is assigned thereto, and with fuel gas via a gas conveyor line ( 62, 63 ), wherein a fuel mixture of combustible dust and combustible gas is provided prior to a moment of ignition of a burner, wherein a first composition of combustible dust and combustible gas, with which a first burner is charged for ignition, is regulated as a function of the fuel quantity, which was supplied to the second burner for ignition, after the ignition of a second burner, which is charged with a second composition of combustible dust and combustible gas for ignition, following the ignition of the first burner, so that the starting up of each of the plurality of burners of the gasifying reactor takes place under a regulated supply of the fuel load. The invention further relates to a gasifying reactor ( 7 ) for carrying out the method according to the invention.

First claim

The invention claimed is:

1. A method for starting up a gasifying reactor that includes a plurality of burners, wherein each burner is charged with combustible dust from a metering vessel via a dense flow conveyor line, which is assigned thereto, and with combustible gas via a gas conveyor line, wherein a fuel mixture of combustible dust and combustible gas is provided prior to a moment of ignition of a burner, the method comprising:
charging a first one of the burners with a first fuel load having a first composition, the first composition being based on a combustible dust flow and a combustible gas flow to ignite the first burner;
charging a second one of the burners with a second fuel load having a second composition, the second composition being based on a combustible dust flow and a combustible gas flow to ignite the second burner after igniting the first one of the burners; and
decreasing the fuel load to the first burner in response to igniting of the second burner to generate synthesis gas gradually by modifying the first composition to obtain a modified first composition, the modified first composition including a combustible dust flow and a combustible gas flow and being modified based on the second fuel load supplied to the second burner for ignition and in response to the ignition of the second burner, the modified first composition being different than the first composition,
wherein the combustible gas flow in the first composition is reduced when the second burner is ignited.

2. The method according to claim 1 , further comprising supplying a third fuel load having a third composition of combustible dust and combustible gas to a third burner in the plurality of burners; igniting the third fuel load; modifying the second composition in response to igniting of the third composition.

3. The method according to claim 1 , wherein the combustible gas is supplied into the corresponding dense flow conveyor line via at least one admixing device located between the metering vessel and the respective burner.

4. The method according to claim 1 , wherein the combustible gas is supplied directly to a supply opening of the burner via at least one admixing device parallel to the dense flow conveyor line via a combustible gas conveyor line.

5. The method according to claim 1 , wherein a combustible dust flow regulating device, which regulates the combustible dust load in the dense flow conveyor line, is in operative connection with the admixing devices for the combustible gas.

6. The method according to claim 1 , wherein all of the individual burners of the plurality of burners are ignited successively, and wherein the fuel load for each burner is no more than 40% of its maximum load.

7. The method according to claim 6 , wherein during the starting up of the individual burners
a combustible dust load is adjusted up to 40% of the maximum load of each burner.

8. The method according to claim 6 , wherein the fuel load for each burner is no more than 30% of its maximum load.

9. The method according to claim 1 , wherein the gasifying reactor is charged with combustible dust from of a solid fuel.

10. The method according to claim 9 , wherein the solid fuel is selected from a group consisting of coal ignite, coke and coke of biomass.

11. The method according to claim 1 , wherein the gasifying reactor yields an output in a range of from 200 MW to 1500 MW.

12. The method according to claim 1 , wherein a flow speed of the combustible dust lies in the range of from 2 to 4 m/s.

13. A gasifying reactor device comprising a plurality of burners; at least one metering vessel; and a plurality of dense flow conveyor lines for supplying combustible dust, each dense flow conveyor line supplying combustible dust to a respective one of the burners,
a combustible dust flow regulating device for regulating a combustible dust flow rate arranged in or on each dense flow conveyor line in operative connection with the dense flow conveyor line of each respective burner;
at least one admixing device for a combustible gas arranged upstream of each burner or on the burner on each dense flow conveyor line; and
a control and regulating unit to adjust supply of fuel load to each burner, each fuel load having a composition based on a combustible dust flow and a combustible gas flow;
wherein the combustible dust regulating devices and the admixing devices are in operative connection with one another, and wherein the control and regulating unit decreases the supply of fuel load by modifying the composition to each burner based on fuel load supplied to a burner located downstream and in response to ignition of the burner located downstream,
wherein the modified composition for each burner includes a combustible dust flow and a combustible gas flow, and for each burner the combustible gas flow of the modified composition is reduced relative to the combustible gas flow of the composition for the burner.

14. The device according to claim 13 , wherein the admixing device for combustible gas is arranged in the corresponding dense flow conveyor line or on a supply opening of the burner.

15. The device according to claim 13 , wherein a combustible gas conveyor line for supplying combustible gas into the admixing device is arranged separated from and close to, in particular parallel to the dense flow conveyor line.

16. The device according to claim 13 , wherein the dust flow regulating device, which is arranged in each dense flow conveyor line and the admixing device for combustible gas, which is assigned to each burner, are operatively connected to one another, wherein the operative coupling forms a regulation of the total fuel load of combustible dust and combustible gas supplied to the burners into the gasifying reactor in response to the ignition of further burners.

17. The method according to claim 1 , wherein the gasifying reactor yields an output in a range of 200 MW to 500 MW.

18. The method according to claim 1 , wherein the combustible gas comprises natural gas with a methane content of more than 50% by volume.

19. The method according to claim 1 , wherein the combustible gas comprises natural gas with a methane content of more than 60% volume.

20. A method for starting up a gasifying reactor that includes a plurality of burners, wherein
each burner is charged with combustible dust from a metering vessel via a dense flow conveyor line, which is assigned thereto, and with combustible gas via a gas conveyor line, wherein a fuel mixture of combustible dust and combustible gas is provided prior to a moment of ignition of a burner, the method comprising:
charging a first one of the burners with a first fuel load having a first composition, the first composition being based on a combustible dust flow and a combustible gas flow to ignite the first burner, the first fuel load being no more than 40% of maximum load of the first burner;
charging a second one of the burners with a second fuel load having a second composition, the second composition including a combustible dust flow and a combustible gas flow to ignite the second burner after igniting the first one of the burners, the second fuel load being no more than 40% of maximum load of the second burner; and
decreasing the fuel load to the first burner in response to igniting of the second burner to generate synthesis gas gradually by modifying the first composition to obtain a modified first composition, the modified first composition being based on a combustible dust flow and a combustible gas flow and being

Assignees

• Schulze Olaf
• Althapp Anton
• Gätke Michael
• Möller Burkhard
• Grunwald Reinhold
• Rabe Wolfgang
• SCHOLZ GüNTER
• Siemens Ag

Inventors

• Schulze Olaf
• Althapp Anton
• Gätke Michael
• Möller Burkhard
• Grunwald Reinhold
• Rabe Wolfgang
• SCHOLZ GüNTER

Classifications

• C10J3/30 Primary

  Fuel charging devices · CPC title

• C10J2200/152

  Nozzles or lances for introducing gas, liquids or suspensions · CPC title

• C10J2300/0933

  Coal fines for producing water gas · CPC title

• C10J2300/1223

  by burners · CPC title

• C10J3/723

  Controlling or regulating the gasification process · CPC title