Method and apparatus for controlling a gasifier

• US 4,489,562 A
• Filed: 11/08/1982
• Issued: 12/25/1984
• Est. Priority Date: 11/08/1982
• Status: Expired due to Fees

• Current Assignee: Combustion Engineering Incorporated (ABB Limited)
• Original Assignee: Combustion Engineering Incorporated (ABB Limited)
• Inventors: Chase, Paul H., Snyder, Troxell K.
• Primary Examiner(s): Woo, Jay H.
• Assistant Examiner(s): Woodard, Joye L.
• Application Number:
  US06/439,969
• Time in Patent Office: 778 Days
• Field of Search: 60/39.12, 60/39.182, 60/648, 60/664, 60/665, 60/667, 48/197 R, 48/202, 48/86, 48/87, 48/61, 48/62 R, 48/77, 48/DIG. 10, 290/40 R, 422/62
• US Class Current: 60/667
• CPC Class Codes: C10J 2300/093 Coal
• CPC Class Codes: C10J 2300/0956 Air or oxygen enriched air
• CPC Class Codes: C10J 2300/1671 with the production of electricity
• CPC Class Codes: C10J 2300/1675 making use of a steam turbine
• CPC Class Codes: C10J 2300/1807 Recycle loops, e.g. gas, solids, heating medium, water
• CPC Class Codes: C10J 2300/1884 with one stream being synthesis gas
• CPC Class Codes: C10J 2300/1892 with one stream being water/steam
• CPC Class Codes: C10J 3/08 with ash-removal in liquid state
• CPC Class Codes: C10J 3/30 Fuel charging devices
• CPC Class Codes: C10J 3/723 Controlling or regulating the gasification process
• CPC Class Codes: F01K 23/067 the combustion heat coming from a gasification or pyrolysis process, e.g. coal gasification gas turbines with fuel gasifiers F02C3/28
• CPC Class Codes: F01K 23/101 Regulating means specially adapted therefor F01K23/105, F01K23/108 take precedence
• CPC Class Codes: Y02E 20/18 Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
• CPC Class Codes: Y10S 48/10 Computer resisted control

Abstract

Fuel and oxidant feed rates into a gasifier 202 are regulated by monitoring overall output 14 and comparing with a pre-selected setpoint valve 10. An overall load demand signal 50, responsive to this comparision is generated and used as an input to control 102 oxidant feed rate. The heating value of the product gas is measured 76 and used to control 64 overall fuel feed rate to the gasifier 202. For a two stage slagging gasifier, the present invention controls 114 fuel feed rate to the slagging stage 210 responsive to the measured slagging stage reaction temperature 128.

Claims

1. A method for controlling the feed rate of fuel and the feed rate of oxidant into a gasifier for producing a product fuel gas, wherein a portion of the energy output of said gasifier is employed to generate steam for driving a steam turbine for the production of electric power, comprising the steps of:

throttling said steam turbine to achieve a desired electrical output level;

determining a desired product gas heating value as a function of a load demand signal;

measuring the actual product gas heating value;

measuring the pressure of the unthrottled steam;

comparing the measured steam pressure with a predetermined pressure setpoint;

generating the load demand signal responsive to any difference between the measured steam pressure and the predetermined setpoint;

comparing the desired and actual product gas heating values;

adjusting the fuel feed rate into said gasifier to compensate for any difference between the measured and the actual product gas heating values;

adjusting the oxidant feed rate into said gasifier in response to the load demand signal.

2. The method of claim 1 wherein the mechanical output of said steam turbine drives an electric generator for producing electric power, further comprising the steps of:

measuring the electric power output of said electric generator;

comparing the measured electric output with the predetermined electric output setpoint; and

throttling said steam turbine to compensate for any difference between the measured output and the output setpoint.

3. An apparatus for controlling the feed rate of fuel and the feed rate of oxidant into a gasifier for producing a product fuel gas, wherein a portion of the energy output of said gasifier is employed to generate steam for driving a steam turbine for producing electric power, comprising:

a throttle for regulating said steam turbine for producing a desired amount of electric power;

means for generating a signal commensurate with the desired product gas heating value in response to a load demand signal;

means for generating a signal commensurate with the actual product gas heating value;

means responsive to the desired and actual heating value signals for generating a heating value error signal;

means responsive to the heating value error signal for adjusting the fuel feed rate;

means for generating a signal commensurate with the pressure of said steam at a location upstream of said throttle;

means responsive to the pressure signal and a desired pressure setpoint for generating a pressure error signal;

means responsive to the pressure error signal for generating the load demand signal; and

means responsive to the load demand signal for adjusting said oxidant feed rate.

4. The apparatus of claim 3 wherein the mechanical output of said steam turbine drives an electric generator for producing electric power, further comprising:

means for generating a signal commensurate with the electric power output of said generator;

means responsive to the power output signal and a predetermined power output setpoint for generating a power output error signal; and

means responsive to the power output error signal for throttling said steam turbine.

5. A method of controlling the fuel feed rate and oxidant feed rate into a two stage slagging gasifier wherein both the oxidant and a first portion of the fuel are fed into the first, slagging stage and second portion of fuel is also fed into the second, reductor stage comprising the steps of:

supplying a gasifier load demand signal;

determining a desired product gas heating value responsive to the load demand signal;

measuring the actual product gas heating value;

determining a desired first stage reaction temperature responsive to on the load demand signal and the slagging characteristics of the fuel;

measuring the actual first stage reaction temperature;

adjusting the oxidant feed rate responsive to the load demand signal;

comparing the actual and the desired first stage reaction temperatures;

adjusting the first stage fuel feed rate to compensate for any difference between the actual and the desired temperatures;

comparing the actual and the desired product gas heating values; and

adjusting the second stage fuel feed rate to compensate for any difference between the actual and the desired heating values.

6. The method of claim 5, wherein a portion of the energy output of said gasifier is used to produce steam for a throttle steam turbine and wherein the step of supplying a load demand signal includes the steps of:

measuring the pressure of the unthrottled steam;

comparing the measured pressure with a predetermined pressure setpoint; and

generating a load demand signal responsive to the difference the measured pressure and the predetermined pressure setpoint.

7. The method of claim 6 wherein the mechanical output of said steam turbine drives an electric generator for producing electric power, further comprising the steps of:

measuring the electric power output of said electric generator;

comparing the measured electric output with a predetermined electric output setpoint; and

throttling said steam turbine to compensate for any difference between the measured output and the output setpoint.

8. Apparatus for controlling the feed rate of fuel and the feed rate of oxidant into a two stage slagging gasifier wherein the oxidant and a first portion of the fuel are feed into the first, slagging stage and a second portion of the fuel is feed into a second, reductor stage, comprising:

means for generating a gasifier load demand signal;

means responsive to the load demand signal for generating a signal commensurate with a desired product gas heating value;

means for generating a signal commensurate with the actual product gas heating value;

10. The apparatus of claim 8, wherein a portion of the energy output of said gasifier is used to produce steam for a throttled steam turbine and wherein the means for generating the load demand signal further comprises:

means for generating a signal commensurate with the pressure of said steam upstream of said throttled steam turbine;

means responsive to the pressure signal and to a predetermined pressure setpoint for generating a pressure error signal; and

means responsive to the pressure error signal for generating the load demand signal.

9. means responsive to the load demand signal and the slagging characteristics of said fuel for generating a signal commensurate with a desired first stage reaction temperature;

means for generating a signal commensurate with the actual first stage reaction temperature;

means responsive to the load demand signal for adjusting the oxidant feed rate;

means responsive to the actual and the desired first stage reaction temperature signals for generating a temperature error signal;

means responsive to the temperature error signal for adjusting the feed rate of said first portion of the fuel into said first stage;

means responsive to the actual and the desired product gas heating value signals for generating a heating value error signal; and

means responsive to the heating value error signal for adjusting the feed rate of said second portion of the fuel into said second stage.

11. The apparatus of claim 9, wherein the mechanical output of said steam turbine drives an electric generator for producing electric power, further comprising:

means for generating a signal commensurate with the electric power output of said generator;

means responsive to the power output signal and a predetermined power output setpoint for generating a power output error signal; and

means responsive to the power output error signal for throttling said steam turbine.