Method for starting high-performance entrained flow gasification reactors with combination burner and multiple burner array

Abstract

A method for starting high-performance entrained flow gasification reactors with a combination burner or a plurality of pulverized fuel burners, and an ignition and pilot burner. The ignition and pilot burner is ignited, substoichiometrically with fuel gas and a gasifier containing free oxygen. The reactor is brought to the pressure intended and a flow of a fuel gas is supplied with a partial flow of the gasification agent at a substoichiometric ratio through the fuel lines leading to the fuel burner and ignited by the flame of the ignition and pilot burner with a partial flow of the gasification agent. Next, the pulverized fuel is supplied together with a further oxygen-containing gasifying agent through the supply lines to the pulverized fuel burner and is ignited by the flame of the ignition and pilot burner and by the fuel gas flames of the combustible gas generated at the pulverized fuel burner.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

Other objects and features of the present invention will become apparent from the following detailed description considered in connection with the accompanying drawings. It is to be understood, however, that the drawings are designed as an illustration only and not as a definition of the limits of the invention.

In the drawings, wherein similar reference characters denote similar elements throughout the several views:

FIG. 1 shows a pulverized fuel feeder vessel with pulverized fuel supply lines for supplying pulverized fuel to the gasification reactor having a combination burner; and

FIG. 2 shows a pulverized fuel feeder vessel with pulverized fuel supply lines for supplying pulverized fuel to the gasification reactor having a multiple burner array.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

The first example intended to provide a better understanding of the invention is a gasification reactor with a combination burner as shown in FIG. 1. The combination burner, which is attached to the head of reactor 2, consists of the ignition and pilot burner with ignition device 2.3 and pulverized fuel burner part 2.4. For supplying the pulverized fuel burner with pulverized fuel, the amount of pulverized fuel needed is supplied through three supply lines 1.2 from a feeder vessel 1.1.

With a gasification reactor 2 with a gross output of 500 MW and combination burner 2.4 described, this corresponds to an amount of pulverized coal of 78 Mg/h. The pulverized fuel has a heating value of 23 MJ/kg. Pulverized fuel is supplied from feeder vessel 1.1 to combination burner 2.4 by means of the three supply lines 1.2 mentioned, that is to say 26 Mg/h per line. The maximum initial output of fuel line 1.2 is 11.7 Mg/h. This initial output results in a minimum ignition heat of 13.5 GJ/h. In the prior art, a minimum ignition heat of 40.5 GJ/h would be necessary at startup.

After the operating pressure in reactor 2 and the ignition output of the ignition and pilot burner 2.3 is achieved, pulverized fuel burner 2.4 is started in such a manner that the automatic control unit causes fuel gas and oxygen-containing gasification agent to be supplied to pulverized fuel burner 2.4 so that the igniting flame of ignition and pilot burner 2.3 first causes a fuel gas-oxygen flame to ignite at each of three pulverized fuel supply lines 1.2. The amount of fuel gas and of oxygen is monitored by a higher order safety system. The sensed heat quantity released by the ignition burner flame and the three combustible fuel gas-oxygen flames at pulverized fuel burner 2.4 is so high that it is ensured that the 11.7 Mg/h pulverized coal flowing into reactor 2 will ignite by means of the automatic control unit causing the first supply line 1.2 to open and the oxygen-containing gasification agent to increase. After that, the second and third pulverized coal supply lines 1.2 are started. The amount of fuel gas, of pulverized coal and of oxygen is monitored by the higher order safety system. Once pulverized coal burner 2.4 has been started, the supply of fuel gas to the pulverized coal burner 2.4 is stopped.

Another example is described with the same burner. Ignition and pilot burner 2.3 is ignited in the same manner as in Example 1. Once the ignition and pilot burner has reached its full output and the desired pressure in gasification reactor 2 has been achieved, the amount of fuel gas corresponding to the necessary minimum ignition heat required of 13.5 MJ/h is added through a pulverized fuel supply pipe 1.2 and ignited with an oxygen-containing gasification agent. Once the flame is stable, the other two pulverized fuel lines 1.2 are immediately brought to react with the solid fuel or slurry and the oxygen-containing oxidation agent. Next, these three pulverized fuel lines 1.2 are adjusted upward to the nominal output of 26 Mg/h per line.

In a third example, the method will be described with gasification reactors having a multiple burner array as shown in FIG. 2. A carbon pulverized coal amount of 240 Mg/h is supplied to a gasification reactor 2 with a gross output of 1.500 MW as shown in FIG. 2. The pulverized fuel has a heating value of 24.7 MJ/kg. At the head of gasification reactor 2 in which the pulverized hard coal is gasified with a gasification agent containing free oxygen, there are mounted an ignition and pilot burner 2.1 and three pulverized coal burners 2.2 that are staggered 120° apart about the ignition and pilot burner. Pulverized coal burners 2.2 are each loaded from one feeder vessel 1.1, each unit supplying ⅓ of the total amount of pulverized fuel, that is 80 Mg/h into reactor 2 by means of three respective supply lines 1.2, that is 26.7 Mg/h per line. The initial output of a supply line 1.2 is 12 Mg/h. Based on this initial output of line 1.2, a minimum ignition heat of only 14.8 GJ/h is needed as compared to the 133.4 GJ/h needed with the prior art method. Once the operating pressure in reactor 2 and the ignition output of the ignition and pilot burner 2.1 are achieved, the three pulverized coal burners 2.2 are started in such a manner that fuel gas and an oxygen-containing gasification agent are supplied to pulverized coal burners 2.2 through the automatic control unit so that the ignition flame of ignition and pilot burner 2.1 causes at first a fuel gas-oxygen flame to ignite at each of the three pulverized coal burners 2.2. The amount of fuel gas and of oxygen is monitored by a higher order safety system. The sensed heat quantity released by the flame of ignition and pilot burner 2.1 and the three fuel gas-oxygen flames at pulverized fuel burners 2.2 is so high that it ensures that the 12 Mg/h pulverized coal flowing into reactor 2 will ignite by means of the automatic control unit, causing first supply line 1.2 to open and the oxygen-containing gasification agent to increase.

Thereafter, a pulverized coal supply line 1.2 of the second pulverized coal burner 2.2 is started with increased gasification agent and then, of the third carbon pulverized coal burner 2.2. Startup is continued in the sequence described until all pulverized coal supply lines 1.2 are in operation. The amount of combustible fuel gas, pulverized coal and oxygen is monitored by the higher order safety system. Once the pulverized coal burners 2.2 are in operation, the supply of fuel gas to pulverized coal burners 2.2 is stopped.

In a fourth embodiment, gasification reactor 2 is started with the aid of ignition and pilot burner 2.1 in a manner analogous to example 3. Once the desired operation pressure and full ignition and pilot burner output are achieved, the amount of fuel gas corresponding to a thermal output of 14.8 GJ/h is supplied through one of the three carbon pulverized coal burners 2.2 and burned substoichiometrically. Next, the other two pulverized coal burners 2.2 are started with pulverized coal, one supply pipe 1.2 being first supplied with the minimum amount of pulverized fuel of 12 Mg/h and then the other two supply pipes 1.2, also with 12 Mg/h each. After burners 2.2 have reached the minimum starting amount of 3×12=36 Mg/h each, they are adjusted upward to the operating performance of 80 Mg/h for each burner 2.2. In a comparable manner, burner 2.2, which is at first supplied with fuel gas, is brought to a performance of 80 Mg/h by stopping the fuel gas supply.

In a fifth embodiment, the method for gasification reactors 2 for slurry gasification having a combination burner and a multiple burner array will be illustrated, as shown in FIG. 2. In place of the dry pneumatic pulverized fuel supply described in examples 1-4, the pulverized fuel for certain fuels such as hard coal, petroleum coke and solid grindable carbon-containing residues can be introduced into the gasification reactor in the form of a pulverized fuel-water or pulverized fuel-oil suspension, called slurry. For a reactor 2 with an output of 500 MW and, as a result thereof, a pulverized fuel need of 78 Mg/h, the amount to be supplied at a solids concentration of 60 wt.-% in the slurry comes up to 130 Mg/h. The minimum ignition heat is 13.56 MJ/h like in Example 1, which corresponds to a slurry amount of 20 Mg/h. The startup process itself takes place as in the previously described examples.

Accordingly, while only a few embodiments of the present invention have been shown and described, it is obvious that many changes and modifications may be made thereunto without departing from the spirit and scope of the invention.

LIST OF THE NUMERALS Used

• 1.1 pulverized fuel feeder vessel
• 1.2 pulverized fuel supply lines
• 2 gasification reactor
• 2.1 ignition and pilot burner
• 2.2 pulverized fuel burner
• 2.3 ignition and pilot burner of the combination burner
• 2.4 pulverized fuel burner of the combination burner

Claims

1. A method for starting a high-performance entrained flow gasification reactor with a combination burner containing an ignition and pilot burner and at least one pulverized fuel burner, for autothermal partial oxidation of pulverized solid fuels such as lignite and hard coal, petroleum coke or solid grindable carbon-containing residues that are pneumatically supplied via pulverized fuel lines to the combination burner with an oxygen-containing gasifying agent at operating pressures of up to 100 bar and temperatures ranging between 1,200° C. and 1,800° C. by means of an ignition flame, the method comprising the following steps: igniting the ignition and pilot burner substoichiometrically with a fuel gas and the oxygen-containing gasifying agent;bringing the entrained flow gasification reactor to a selected pressure of up to 100 bar;supplying a flow of the fuel gas with a partial flow of the oxygen-containing gasifying agent at a substoichiometric ratio through the pulverized fuel lines leading to the pulverized fuel burner;supplying the pulverized fuel together with further oxygen-containing gasifying agents through the pulverized fuel lines to the pulverized fuel burner; andigniting the pulverized fuel by a flame of the ignition and pilot burner and by fuel gas flames at the pulverized fuel burners.

2. The method according to claim 1, wherein the pulverized fuel is supplied as a pulverized fuel-water or pulverized fuel-oil suspension.

3. The method according to claim 1, wherein the fuel gas is introduced through all of the pulverized fuel lines and wherein the pulverized fuel is supplied thereafter.

4. The method according to claim 1, wherein the fuel gas is introduced through one pulverized fuel line only and wherein pulverized fuel is then supplied through all the pulverized fuel lines.

5. The method according to claim 1, wherein an amount of heat needed for ignition of the pulverized fuel is equal to or greater than 0.05 to 0.5 times a product of pulverized fuel mass flow of one supply line only and its heating value.

6. The method as set forth in claim 1, wherein startup of the reactor is monitored by a higher order, independent, automatically acting safety system.