Process for regulating joule value of offgases from plants for pig iron production or of synthesis gas

1. A method for regulating a joule value of offgases from plants having integrated CO 2 removal, where at least one part of pig iron production offgas or synthesis gas from synthesis gas production is discharged as export gas that is subsequently thermally utilized in a gas turbine and offgas from the gas turbine is supplied to a waste heat boiler for generating steam, said method comprising:

adding at least one part of tail gas from the CO 2 removal to the export gas before the gas turbine, based on the joule value of the export gas after the addition of the tail gas, to increase a proportion of tail gas, if the joule value of the export gas rises above a predefined maximum joule value, and to reduce the proportion of tail gas, if the joule value of the export gas drops below a predefined minimum joule value.

2. The method as claimed in claim 1 ,

wherein the export gas is collected in an export gas container upstream of the gas turbine, and

wherein the tail gas is added to the export gas upstream of the export gas container.

3. The method as claimed in claim 1 , wherein the export gas mixed with the tail gas flows through a buffer container before the gas turbine.

4. The method as claimed in claim 3 , further comprising adding gaseous fuel when the predefined minimum joule value is not reached before the gas turbine, at least one of before the buffer container and after the buffer container.

5. The method as claimed in claim 3 , further comprising adding non-combustible gas when the predefined maximum joule value before the gas turbine is exceeded, at least one of before the buffer container and after the buffer container.

6. The method as claimed in claim 5 ,

wherein the export gas is pig iron production offgas, and

wherein the method further comprises supplying a remaining part of the tail gas, not added to the export gas, to one of a smelter gas distribution network and a hot flare.

7. The method as claimed in claim 6 , wherein the remaining part of the tail gas is supplied to a furnace gas distribution network.

8. The method as claimed in claim 5 , wherein the export gas contains at least one of:

top gas from an oxygen blast furnace having top gas recirculation,

smelter gasifier offgas from a smelter gasifier of a smelting reduction plant,

reduction offgas from at least one of a reduction reactor and a reduction shaft of the smelting reduction plant,

reactor offgas from at least one fixed bed reactor to at least one of heat and reduce at least one of iron oxides and compacted iron of the smelting reduction plant, and

the synthesis gas from a synthesis gas production plant.

9. A plant, comprising:

one of a pig iron production plant and a synthesis gas production plant, with an integrated CO 2 sequestration plant;

at least one export gas line discharging a part of pig iron production offgas or synthesis gas as export gas from the pig iron production plant or for synthesis gas production, respectively;

a gas turbine thermally utilizing the export gas;

a waste heat boiler utilizing offgas from the gas turbine for generation of steam;

a measuring instrument measuring a joule value of the export gas; and

a connection between the CO 2 sequestration plant and the export gas line, adding at least one part of tail gas from the CO 2 sequestration plant to the export gas upstream of the gas turbine.

10. The plant as claimed in claim 9 ,

further comprising an export gas container collecting the export gas upstream of the gas turbine,

wherein the connection between the CO 2 sequestration plant and the export gas line is upstream of the export gas container, and

wherein the measuring instrument is provided after the export gas container.

11. The plant as claimed in claim 10 , further comprising a buffer container provided after the export gas container and before the gas turbine.

12. The plant as claimed in claim 11 , further comprising at least one fuel supply line supplying gaseous fuel at least one of before and after the buffer container.

13. The plant as claimed in claim 12 , further comprising at least one gas supply line supplying non-combustible gas at least one of before and after the buffer container.

14. The plant as claimed in claim 13 ,

wherein the pig iron production plant produces the export gas and has a smelter gas distribution network, and

wherein the plant further comprises a tail gas line supplying a remaining part of the tail gas, not added to the export gas, to the smelter gas distribution network.

15. The plant as claimed in claim 14 , wherein the smelter gas distribution network is a furnace gas distribution network.

16. The plant as claimed in claim 13 ,

wherein the pig iron production plant produces the export gas, and

wherein the plant further comprises a tail gas line supplying a remaining part of the tail gas, not added to the export gas, to a hot flare.

17. The plant as claimed in claim 13 , wherein the at least one export gas line includes at least one of

a top gas line from an oxygen blast furnace having top gas recirculation,

a smelter gasifier offgas line from a smelting gasifier of a smelting reduction plant,

a reduction offgas line from at least one of a reduction reactor and a reduction shaft of the smelting reduction plant,

a reactor offgas line from at least one fixed bed reactor heating and reducing iron oxides and/or compacted iron in the smelting reduction plant, and

a synthesis gas line from the synthesis gas production plant.