Title of Invention	GAS AND STEAM TURBINE UNIT
Abstract	This invention relates to a gas and steam turbine plant (1) comprising a steam generator (30) which uses waste heat and is mounted downstream from the gas turbine (2) on the flue gas side. The heating surfaces of the generator are mounted in the water-steam circuit (24) of said steam turbine (20). A gasification device (132) is mounted downstream from the gas turbine (2) through a fuel duct (130) for integrated gasification of a fossil fuel (B). A saturator (150) is mounted in the fuel duct (130). Reliable operation of said saturator (150) is required for such a gas and steam turbine unit (1) irrespective of the operation mode of said gasification device (132). In addition, a steam water-heat exchanger (184), mounted on the secondary side statutory circuit (132),is fed on its primary side with feeding water (S) drawn from the water steam circuit (24) of the steam turbine (20). The feed water (S) which is cooled in the water-heat exchanger of the saturator (184) can be heated by means of a partial stream (T) of compressed air, whereby said partial stream (T) of compressed air can be transferred to an air separation facility (138) mounted upstream from said gasification device.

Title of Invention

GAS AND STEAM TURBINE UNIT

Abstract

This invention relates to a gas and steam turbine plant (1) comprising a steam generator (30) which uses waste heat and is mounted downstream from the gas turbine (2) on the flue gas side. The heating surfaces of the generator are mounted in the water-steam circuit (24) of said steam turbine (20). A gasification device (132) is mounted downstream from the gas turbine (2) through a fuel duct (130) for integrated gasification of a fossil fuel (B). A saturator (150) is mounted in the fuel duct (130). Reliable operation of said saturator (150) is required for such a gas and steam turbine unit (1) irrespective of the operation mode of said gasification device (132). In addition, a steam water-heat exchanger (184), mounted on the secondary side statutory circuit (132),is fed on its primary side with feeding water (S) drawn from the water steam circuit (24) of the steam turbine (20). The feed water (S) which is cooled in the water-heat exchanger of the saturator (184) can be heated by means of a partial stream (T) of compressed air, whereby said partial stream (T) of compressed air can be transferred to an air separation facility (138) mounted upstream from said gasification device.

Full Text	The invention relates to a gas turbine and steam turbine with a waste-heat steam generator whose flue 'gas side is connected downstream of a gas turbine, the heating surfaces of which waste-heat steam generator being connected into the water/steam cycle of a steam turbine, and having a gasification device, for fuel, connected upstream of the combustion chamber of the gas turbine by means of a fuel line, a saturator, in which the gasified fuel is guided in counterflow to a water flow guided in a saturator cycle, being connected into the fuel line. A gas turbine and steam turbine installation with integrated gasification of fossil fuel usually comprises a fuel gasification device which is connected, at the outlet end, to the combustion chamber of the gas turbine via a number of components provided for gas cleaning. The flue gas side of a waste-heat steam generator can then be connected downstream of the gas turbine, the heating surfaces of which waste-heat steam generator being connected into the water/steam cycle of the steam turbine. Such an installation is known, for example, from GB-A 2 234 984. In order to reduce" the pollutant emission during the combustion of the gasified fossil fuel, a saturator is connected, in this installation, into the fuel line between the gasification device and the combustion chamber of the gas turbine. The gasified fuel is charged with water vapour in the saturator. For this purpose, the gasified fuel flows through the saturator in counterflow to a flow of water which is guided within a water cycle which is designated the saturator cycle. In order to set a temperature level in the saturator which is sufficient for charging the gasified fuel with water vapour, heat is coupled into the saturator cycle by cooling the tapped air and/or by cooling the crude gas from the fuel gasification. 3 In this installation, however, the operation of the saturator depends on the operating condition of the gasification device and/or on the operating condition of an air separation installation connected upstream of the gasification device, so that this concept only has limited flexibility. With respect to control, furthermore, such a concept is comparatively complicated and therefore susceptible to failure. In this connection, it is known from US 5,319,924 to preheat in a heat exchanger the feed water to be fed into a saturator, it being possible to subject the heat exchanger with uncleaned crude gas on the primary side. In addition, a saturator configured as a fuel humidifier is known from DE 43 21 081 in which a heat exchanger, which is subjected to feed water on the primary side, is provided for preheating the saturator water. In the article "Effiziente und umweltfreundliche Stromerzeugung im GUD-Kraftwerk mit integrierter Vergasung" [Efficient and environmentally friendly power production in a gas and steam power plant with integrated gasification] by G. Haupt in "Elektrotechnik und Informationstechnik" [Electrical engineering and information technology] ,AT Springer Verlag, Vienna, Volume 113, No. 1,2 (February 1996), pages 102-105, the heating in a heat exchanger of a water flow which is to be fed into a saturator is described. The water flow is heated in a heat exchange with feed water extracted from the water/steam cycle of the steam turbine and supplied in a dedicated reservoir ("flash tank") connected into a circulating circuit. A heat exchanger is connected into this circulating circuit and in said heat exchanger the feed water absorbs heat from air compressed by a partial flow, the air being appropriately cooled in the process. The invention is therefore based on the object of providing a gas turbine and steam turbine AMENDED SHEET installation of the type mentioned above which permits, in a particularly simple manner, reliable operation of the saturator even under different operating conditions. 5 In accordance with the invention, this object is achieved by a saturator-water heat exchanger, which is connected on the secondary side into the saturator cycle to heat the water flow, being capable of being subjected, on the primary side, to feed water extracted from the water/steam cycle of the steam turbine, it being possible to heat the feed water cooled in the saturator-water heat exchanger by means of a partial flow of compressed air, It being possible to supply the partial flow of compressed air to an air separation installation connected upstream of the gasification device, and it being possible to connect a further heat exchanger on the primary side in a tapped air line connecting the air compressor to the air separation installation in order to cool the partial flow of compressed air, the secondary side of which further heat exchanger is connected into a feed water line connecting the saturator-water heat exchanger at the outlet end to a feed water tank associated with the waste-heat steam generator. The invention is based on the consideration that reliable operation of the saturator is also made possible at various operating conditions, and therefore particularly high flexibility of the gas turbine and steam turbine installation, in that the saturator^ 6 can be operated independently of the operating parameters of the gasification device and the air separation installation. In this connection, the coupling of the heat into the saturator cycle, in particular, should not take place directly by means of a medium flowing out of the gasification device or by means of tapped air flowing into the air separation installation. Instead of this, coupling of heat into the saturator cycle is, rather, provided by means of a medium extracted from the water/steam cycle of the steam turbine, it being possible for the operating parameters for the gasification device and/or the air separation installation, on the one hand, and the saturator, on the other, to be set independently of one another. The control devices necessary for operating these components can also, therefore, be comparatively simply constructed. In a particularly advantageous further development, oxygen from an air separation installation can be supplied to the gasification device, which air separation installation can, for its part, be subjected at the inlet end to a partial flow of air compressed in an air compressor associated with the . gas turbine, a further heat exchanger being connected on the primary side in a tapped air line connecting the air compressor to the air separation installation in order to cool the partial flow of compressed air, the secondary side of which further heat exchanger is connected into a feed water line connecting the saturator-water heat exchanger at the output end to a feed water line associated with the waste-heat steam generator. Such an arrangement ensures a particularly high installation efficiency. The feed water flowing to the saturator-water heat exchanger is initially cooled by the thermal coupling into the water flow guided in the saturator cycle. In the further heat exchanger connected on the feed water side downstream of the saturator-water heat exchanger, the cooled feed water then experiences 7 reheating, cooling, of the partial flow of compressed air, also referred to as tapped air, flowing to the air separation installation, taking place simultaneously. Coupling of heat from the tapped air flow into the water/steam cycle of the steam turbine therefore occurs to provide a particularly large , 8 recovery of heat. In order to compensate for losses in the water flow guided in the saturator cycle, for example because of the charging of the gasified fuel with water vapour in the saturator, a feed line expediently opens into the saturator cycle, the entry location of the feed line into the saturator cycle being provided before the saturator-water heat exchanger, viewed in the flow direction of the water flow, in order to provide a particularly high installation efficiency in a particularly advantageous embodiment. With such an arrangement, a particularly high transfer of heat from the feed water to the water flow guided in the saturator cycle is ensured. The feed water therefore flows out of the saturator-water heat exchanger with a particularly low temperature so that, particularly when the cooled feed water is used for cooling the tapped air, a particularly effective cooling of the tapped air is also made possible. The advantages achieved by the invention consist in particular in the fact that because of the coupling of heat into the saturator cycle by means of feed water extracted from the water/steam cycle of the steam turbine, reliable operation of the saturator is made possible independent of the operating condition of the gasification device. In consequence, the gas turbine in particular can also be operated within specified parameter limits independent of the operating condition of the gasification device. Such a concept for coupling in heat is therefore particularly flexible and, in particular, is. also independent of the integration concept, i.e. independent of the type of air supply for the air separation installation and the components employed for that purpose. Because of the use of the feed water, cooled due to the heat transfer to the water flow, for cooling the tapped air from the air separation installation, a particularly high installation efficiency is also ensured. 9 An embodiment example of the invention is explained in more detail using an accompanying drawing. The figure in the drawing shows, diagrammatically, a gas turbine and steam turbine installation. The gas turbine and steam turbine installation 1 shown in the figure comprises a gas turbine installation la and a steam turbine installation lb. The gas turbine installation la comprises a gas turbine 2 with, connected to it, an air compressor 4 and a combustion chamber 6, which is connected upstream of the gas turbine 2 and is connected to a compressed air line 8 of the compressor 4. The gas turbine 2, the air compressor 4 and a generator 10 are located on a common shaft 12. The steam turbine installation lb comprises a steam turbine 2 0 with, coupled to it, a generator 2 2 and, in a water/steam cycle 24, a condenser 2 6 and a waste-heat steam generator 30 connected downstream of the steam turbine 20. The steam turbine 20 consists of a first pressure stage or a high-pressure part 20a and a second pressure stage or a medium-pressure part 2 0b and a third pressure stage or a low-pressure part 20c, which drive the generator 22 via a common shaft 32. An exhaust gas line 3 4 is connected to an inlet 3 0a of the waste-heat steam generator 30 in order to feed working medium AM or flue gas expanded in the gas turbine 2 into the waste-heat steam generator 30. The expanded working medium AM from the gas turbine 2 leaves the waste-heat steam generator 3 0 via its outlet 3 0b in the direction of a chimney (not shown in any more detail). The waste-heat steam generator 3 0 comprises a condensate preheater 40 which can be fed, at its inlet end, with condensate K from the condenser 2 6 via a condensate line 42, into which is connected a condensate pump unit 44. At its outlet end, the condensate preheater 4 0 is connected via a line 45 to a feed water tank 46. In order, if required, to bypass 10 the condensate preheater 40, the condensate line 42 can, in addition, be connected directly to the feed water tank 46 via a bypass line {not shown). The feed water tank 46 is connected via a line 47 to a high-pressure feed pump 48, with medium pressure extraction. The high-pressure feed pump 48 brings the feed water S flowing from the feed water tank 46 to a pressure level suitable for a high-pressure stage 50 of the water/steam cycle 24 associated with the high-pressure part of the steam turbine 20. The feed water S which is at a high pressure - can be supplied to the high-pressure stage 50 via a feed water preheater 52 which, at its outlet end, is connected to a high-pressure drum 58 via a feed water line 56 which can be shut off by a valve 54. The high-pressure drum 5 8 is connected to a high-pressure evaporator 60 arranged in the waste-heat steam generator 30 for the formation of a water/steam circuit 62. For the removal of the live steam F, the high-pressure drum 58 is connected to a high-pressure superheater 64 arranged in the waste-heat steam generator 30, the high-pressure superheater 64 being connected at its outlet end to the steam inlet 66 of the high-pressure part 20a of the steam turbine 20. The steam outlet 68 of the high-pressure part 20a of the steam turbine 20 is connected via a reheater 70 to the steam inlet 72 of the medium-pressure part 20b of the steam turbine 20. The steam outlet 74 of the medium-pressure part 20b is connected via a transfer line 76 to the steam inlet 78 of the low-pressure part 20c of the steam turbine 20. The steam outlet 80 of the low-pressure part 20c of the steam turbine 20 is connected via a steam line 82 to the condenser 2 6 so that a closed water/steam cycle 24 results. In addition, a branch line 84 branches off from the high-pressure feed pump 48 at an extraction location at which the condensate K has reached a medium 11 pressure. This branch line 84 is connected via a further feed water preheater 86 or medium-pressure economizer to a 12 medium-pressure stage 9 0 of the water/steam cycle associated with a medium-pressure part 20b of the steam turbine 20. For this purpose, the second feed water preheater 86 is connected at its outlet end via a feed water line 94, which can be shut off by a valve 92, to a medium-pressure drum 96 of the medium-pressure stage 90. The medium-pressure drum 96 is connected to a heating surface 98 arranged in the waste-heat steam generator 3 0 and configured as a medium-pressure evaporator in order to form a water/steam circuit 100. For the removal of medium-pressure live steam F , the medium-pressure drum 96 is connected via a steam line 102 to the reheater 70 and therefore to the steam inlet 72 of the medium-pressure part 2 0b of the steam turbine 20. A further line 110, which is provided with a low-pressure feed pump 107, which can be shut off by a valve 108 and which is connected to a low-pressure stage 120 of the water/steam cycle 24 associated with the low-pressure part 20c of the steam turbine 20, branches off from the line 47. The low-pressure stage 12 0 comprises a low-pressure drum 122, which is connected, in order to form a water/steam circuit 12 6, to a heating surface 124 arranged in the waste-heat steam generator 3 0 and configured as a low-pressure evaporator. In order to remove low-pressure live steam F", the low-pressure drum 122 is connected to the transfer line 76 via a steam line 128, into which is connected a low-pressure superheater 129. The water/steam cycle 24 of the gas turbine and steam turbine installation 1 therefore comprises, in the embodiment example, three pressure stages 50, 90, 120. As an alternative, however, fewer pressure stages, in particular two, can be provided. The gas turbine installation la is configured for operation with a gasified synthesis gas SG which is generated by the gasification of a fossil fuel B. Gasified coal or gasified oil can, for example, be 13 provided as the synthesis gas. For this purpose, the combustion chamber 6 of the gas turbine 2 is connected at its inlet end via a fuel line 130 to a gasification device 132. Coal or oil, as the fossil fuel B, can be supplied to the gasification device 132 14 via a charge system 134. In order to make available the oxygen 02 necessary for the gasification of the fossil fuel B, an air separation installation 13 8 is connected via an oxygen line 13 6 upstream of the gasification device 132. At its inlet end, the air separation installation 13 8 can be subjected to a partial flow T of the air compressed in the air compressor 4. For this purpose, the air separation installation 138 is connected, at its inlet end, to a tapped air line 140 which branches off from the compressed air line 8 at a branch location 142. A further air line 143, into which is connected an additional air compressor 144, also opens into the tapped air line 140. In the embodiment example, the total airflow L flowing to the air separation installation 138 is made up of the partial flow T branched off from the compressed air line 8 and the airflow delivered by the additional air compressor 144. Such a connection concept is also designated a partially integrated installation concept. In an alternative embodiment, the so-called fully integrated installation concept, it is possible to dispense with the further air line 143 and also with the additional air compressor 14 4 so that the complete air feed to the air separation installation 138 takes place by means of the partial flow T extracted from the compressed air line 8. The nitrogen N2 obtained, in addition to the oxygen O2, in the air separation installation 138 during the separation of the airflow L is supplied to a mixing appliance 146, via a nitrogen line 145 connected to the air separation installation 138, and is there mixed with the synthesis gas SG. The mixing appliance 146 is then configured for a particularly uniform and streak-free mixing of the nitrogen N2 with the synthesis gas SG. The synthesis gas SG flowing away from the gasification device 132 passes initially, via the fuel line 130, into a 15 crude gas waste-heat steam generator 14 7 in which, by means of heat exchange with a flow medium, cooling of the synthesis gas SG takes place. High-pressure steam generated during this heat exchange is supplied, in a manner not shown in any more detail, to the high-pressure stage 50 of the water/steam cycle 24. Behind the crude gas waste-heat steam generator 14 7 and before the mixing appliance 14 6, viewed in the flow direction of the synthesis gas SG, a dust-removal device 148 for the synthesis gas SG and a desulphurization installation 149 are connected into the fuel line 130. In an alternative configuration, a soot-washing appliance can also be provided instead of the dust-removal device 148, in particular in the case of the gasification of oil as the fuel. For particularly low pollutant emission during the combustion of the gasified fuel in the combustion chamber 6, the gasified fuel is charged with water vapour before it enters into the combustion chamber 6. This can take place in a thermally particularly advantageous manner in a saturator system. For this purpose, a saturator 150, in which the gasified fuel is guided in counterflow relative to the heated water flow W (also referred to as saturator water), is connected into the fuel line 13 0. The saturator water or the water flow W then circulates in a saturator cycle 152, which is connected to the saturator 150 and into which a circulating pump 154 is connected. A feed line 158 is connected to the saturator cycle 152 to compensate for losses of saturator water occurring during the saturation of the gasified fuel. The secondary side of a heat exchanger 159 acting as a crude gas/mixed gas heat exchanger is connected into the fuel line 13 0 behind the saturator 150, viewed in the flow direction of the synthesis gas SG. The primary side of the heat exchanger 159 is then likewise connected into the fuel line 130 at a position 16 in front of the dust removal installation 148, so that the synthesis gas SG flowing to the dust. 17 removal installation 148 transfers a part of its heat to the synthesis gas SG flowing out of the saturator 150. The guidance of the synthesis gas SG via the heat exchanger 159 before it enters the desulphurization installation 149 can then also be provided in a modified connection concept relative to the other components. In the case of the connection of a soot-washing device, in particular, the heat exchanger can preferably be arranged on the crude gas side downstream of the soot-washing device. The secondary side of a further heat exchanger 160, whose primary side can be heated by feed water or also by steam, is connected into the fuel line 130 between the saturator 150 and the heat exchanger 159. Particularly reliable preheating of the synthesis gas SG flowing to the combustion chamber 6 of the gas turbine 2, even in the case of different operating conditions of the gas turbine and the steam turbine installation 1, is then ensured by the heat exchanger 159, which is configured as a crude gas/clean gas heat exchanger, and by the heat exchanger 160. In order to subject the synthesis gas SG flowing to the combustion chamber 6 to steam, if required, a further mixing appliance 161 is, in addition, connected into the fuel line 130. Medium-pressure steam can be supplied to this further mixing appliance 161 via a steam line (not shown in any more detail) in order, in particular, to ensure reliable gas turbine operation in the case of operational faults. In order to cool the partial flow T of compressed air, also designated as tapped air, to be supplied to the air separation installation 13 8, the primary side of a heat exchanger 162 is connected into the tapped air line 140, the secondary side of this heat exchanger 162 being configured as a medium-pressure evaporator for a flow medium S' . The heat exchanger 162 is connected to a water/steam drum 164, which is configured as a medium-pressure drum, in order 18 to form an evaporator circuit 163. The water/steam drum 164 is connected to the medium-pressure drum 96 associated with the water/steam circuit 100 by lines 166, 168. As an alternative, the secondary side of the heat exchanger 162 can also be directly connected to the medium-pressure drum 96. In the embodiment example, the water/steam drum 164 is therefore directly connected to the heating surface 98, which is configured as a medium-pressure evaporator. In addition, a feed water line 170 is connected to the water/steam drum 164 in order to top up evaporated flow medium S'. A further heat exchanger 172, whose secondary side is configured as the low-pressure evaporator for a flow medium S" is connected into the tapped air line 14 0 after the heat exchanger 162, viewed in the flow direction of the partial flow T of compressed air. The heat exchanger 172 is then connected to a water/steam drum 176, which is configured as a low-pressure drum, in order to form an evaporator circuit 174. In the embodiment example, the water/steam drum 176 is connected to the low-pressure drum 122, which is associated with the water/steam circuit 12 6, via lines 178, 180 and is therefore directly connected to the heating surface 124, which is configured as a low-pressure evaporator. As an alternative, however, the water/steam drum 176 can also be connected in another suitable manner, it being then possible to supply steam taken from the water/steam drum 176 to an auxiliary consumption unit as process steam and/or as steam for heating purposes. In a further alternative embodiment, the secondary side of the heat exchanger 172 can also be directly connected to the low-pressure drum 122. The water/steam drum 176 is, in addition, connected to a feed water line 182. Each of the evaporator circuits 163, 174 can be configured as a forced circulation system, the circuit of the flow medium S' or S" being ensured by a circulating pump and the flow medium S', S" being at least partially evaporated in a heat exchanger 162 or 172 configured as an evaporator. In the embodiment 20 example, however, both the evaporator circuit 163 and the evaporator circuit 174 are respectively configured as natural circulation systems, the circulation' of the flow medium S' or . 21 S" being ensured by the pressure differences arising during the evaporation process and/or by the geodetic arrangement of the respective heat exchanger 162 or 172 and the respective water/steam drum 164 or 176. In this configuration, only a comparatively modestly dimensioned circulating pump (not shown) is respectively connected into the evaporator circuit 163 or into the evaporator circuit 174 for starting the system. For the connection of heat into the saturation cycle 152 and therefore for setting a temperature in the water flow W sufficient for charging the synthesis gas SG with water vapour, a saturator-water heat exchanger 184 is provided which can be subjected on the primary side to feed waters from the feed water tank 46. For this purpose, the primary side of the saturator-water heat exchanger 184 is connected/ at the inlet end, via a line 186 to the branch line 84 and, at the outlet end, via a line 188 to the feed water tank 46. The saturator-water heat exchanger 184 is then connected on the secondary side downstream, viewed in the flow direction of the water flow W, of the inlet of the feed line 158 into the saturator cycle 152. For additional heating of the water flow W, if required, an additional heat exchanger 189 is connected into the saturator cycle 152 in the embodiment example. The additional heat exchanger 189 is then subjected on the primary side to preheated feed water from the medium pressure stage 90 of the water/steam cycle 24. The additional heat exchcinger 18 9 can, however, also be dispensed with - depending on the specified emission figures and/or combustion gas temperatures. A further heat exchanger 190 is connected into the line 188 for reheating the cooled feed water S flowing from the saturator-water heat exchanger 184, this further heat exchanger 190 being connected on the primary side downstream of the heat exchanger 172 in the tapped air line 140. Such an arrangement can achieve a 22 particularly high heat, recovery from the tapped air and, therefore, a particularly high efficiency of the gas turbine and steam turbine installation 1. A cooling air line 192, by means of which a partial quantity T' of the cooled partial flow T can be supplied as cooling air to the gas turbine 2 for blade cooling, branches off from the tapped air line 140 between the heat exchanger 172 and the heat exchanger 190, viewed in the flow direction of the partial flow T. Subjecting the saturator-water heat exchanger 184 to feed water S from the water/steam cycle 24 of the steam turbine 20 permits reliable operation of the saturator 150 independent of the operating condition of the air separation installation 138. The overall efficiency of the gas turbine and steam turbine installation 1 then benefits particularly from the fact that reheating of the feed water S cooled in the saturator-water heat exchanger 184 takes place in the additional heat exchanger 190. This ensures reliable setting of the final temperature of the partial flow T flowing as tapped air to the air separation installation 138 with simultaneous recovery of the heat carried in this for the energy generation process of the gas turbine and steam turbine installation 1. 23 We Claim: 1. A gas and steam turbine plant (1) comprising a waste-heat steam generator (30) whose flue gas side is connected downstream of a gas turbine (2), heating surfaces of said waste-heat steam generator (30) being connected to a water/steam cycle (24) of a steam turbine (20); a gasification device (132), for fuel (B), connected upstream of a combustion chamber (6) of the gas turbine (2) by means of a fuel line (130); a saturator (150), in which the gasified fuel ( SG) being guided in counterflow to a water flow (W) guided in a saturator cycle (152), connected into the fuel line ( 130); and a saturator-water heat exchanger (184) connected on the secondary side into the saturator cycle (152) to heat the water flow (W), the primary side of said saturator-water heat exchanger (184) being subjected to feed water (S) extracted from the water/steam cycle (24) of the steam turbine (20), the feed water (S) cooled in the saturator-water heat exchanger (184) being heatable by means of a partial flow (T) of compressed air, the partial flow (T) of compressed air being supplied to an air separation installation (138) connected upstream of the gasification device (132), characterized in that an additional heat exchanger (190) is connected on the primary side in a tapped air line (140) connecting the air compressor (4) to the air separation installation (138) in order to cool the partial flow (T) of compressed air , and in that the secondary side of the additional heat exchanger (190) is connected into a feed water line (188) connecting the saturator-water heat exchanger (184) at the outlet end to a feed water tank (46) associated with the waste-heat steam generator (30). 2. A gas and steam turbine plant (1) as claimed in claim 1, wherein oxygen ( O2 ) from the air separation installation (138) supplied to the gasification device (132), and wherein the air separation installation (138) is capable of being subjected at the inlet end to the partial flow ( T) of air compressed in an air compressor (4) associated with the gas turbine (2). 24 3. A gas and steam turbine plant (1) as claimed in claim 1 or 2, wherein a feed line (158) opens into the saturator cycle (152) before the saturator-water heat exchanger (184) when viewed in the flow direction of the water flow ( W). This invention relates to a gas and steam turbine plant (1) comprising a steam generator (30) which uses waste heat and is mounted downstream from the gas turbine (2) on the flue gas side. The heating surfaces of the generator are mounted in the water-steam circuit (24) of said steam turbine (20). A gasification device (132) is mounted downstream from the gas turbine (2) through a fuel duct (130) for integrated gasification of a fossil fuel (B). A saturator (150) is mounted in the fuel duct (130). Reliable operation of said saturator (150) is required for such a gas and steam turbine unit (1) irrespective of the operation mode of said gasification device (132). In addition, a steam water-heat exchanger (184), mounted on the secondary side statutory circuit (132),is fed on its primary side with feeding water (S) drawn from the water steam circuit (24) of the steam turbine (20). The feed water (S) which is cooled in the water-heat exchanger of the saturator (184) can be heated by means of a partial stream (T) of compressed air, whereby said partial stream (T) of compressed air can be transferred to an air separation facility (138) mounted upstream from said gasification device.

Full Text

The invention relates to a gas turbine and steam turbine with a waste-heat steam generator whose flue 'gas side is connected downstream of a gas turbine, the heating surfaces of which waste-heat steam generator being connected into the water/steam cycle of a steam turbine, and having a gasification device, for fuel, connected upstream of the combustion chamber of the gas turbine by means of a fuel line, a saturator, in which the gasified fuel is guided in counterflow to a water flow guided in a saturator cycle, being connected into the fuel line.
A gas turbine and steam turbine installation with integrated gasification of fossil fuel usually comprises a fuel gasification device which is connected, at the outlet end, to the combustion chamber of the gas turbine via a number of components provided for gas cleaning. The flue gas side of a waste-heat steam generator can then be connected downstream of the gas turbine, the heating surfaces of which waste-heat steam generator being connected into the water/steam cycle of the steam turbine. Such an installation is known, for example, from GB-A 2 234 984.
In order to reduce" the pollutant emission during the combustion of the gasified fossil fuel, a saturator is connected, in this installation, into the fuel line between the gasification device and the combustion chamber of the gas turbine. The gasified fuel is charged with water vapour in the saturator. For this purpose, the gasified fuel flows through the saturator in counterflow to a flow of water which is guided within a water cycle which is designated the saturator cycle. In order to set a temperature level in the saturator which is sufficient for charging the gasified fuel with water vapour, heat is coupled into the saturator cycle by cooling the tapped air and/or by cooling the crude gas from the fuel gasification.

3
In this installation, however, the operation of the saturator depends on the operating condition of the gasification device and/or on the operating condition of an air separation installation connected upstream of the gasification device, so that this concept only has limited flexibility. With respect to control, furthermore, such a concept is comparatively complicated and therefore susceptible to failure.
In this connection, it is known from US 5,319,924 to preheat in a heat exchanger the feed water to be fed into a saturator, it being possible to subject the heat exchanger with uncleaned crude gas on the primary side. In addition, a saturator configured as a fuel humidifier is known from DE 43 21 081 in which a heat exchanger, which is subjected to feed water on the primary side, is provided for preheating the saturator water.
In the article "Effiziente und umweltfreundliche Stromerzeugung im GUD-Kraftwerk mit integrierter Vergasung" [Efficient and environmentally friendly power production in a gas and steam power plant with integrated gasification] by G. Haupt in
"Elektrotechnik und Informationstechnik" [Electrical
engineering and information technology] ,AT Springer Verlag, Vienna, Volume 113, No. 1,2 (February 1996), pages 102-105, the heating in a heat exchanger of a water flow which is to be fed into a saturator is described. The water flow is heated in a heat exchange with feed water extracted from the water/steam cycle of the steam turbine and supplied in a dedicated reservoir ("flash tank") connected into a circulating circuit. A heat exchanger is connected into this circulating circuit and in said heat exchanger the feed water absorbs heat from air compressed by a partial flow, the air being appropriately cooled in the process.
The invention is therefore based on the object of providing a gas turbine and steam turbine
AMENDED SHEET

installation of the type mentioned above which permits, in a particularly simple manner, reliable operation of the saturator even under different operating conditions.

5
In accordance with the invention, this object is achieved by a saturator-water heat exchanger, which is connected on the secondary side into the saturator cycle to heat the water flow, being capable of being subjected, on the primary side, to feed water extracted from the water/steam cycle of the steam turbine, it being possible to heat the feed water cooled in the saturator-water heat exchanger by means of a partial flow of compressed air, It being possible to supply the partial flow of compressed air to an air separation installation connected upstream of the gasification device, and it being possible to connect a further heat exchanger on the primary side in a tapped air line connecting the air compressor to the air separation installation in order to cool the partial flow of compressed air, the secondary side of which further heat exchanger is connected into a feed water line connecting the saturator-water heat exchanger at the outlet end to a feed water tank associated with the waste-heat steam generator.
The invention is based on the consideration that reliable operation of the saturator is also made possible at various operating conditions, and therefore particularly high flexibility of the gas turbine and steam turbine installation, in that the saturator^

6
can be operated independently of the operating parameters of the gasification device and the air separation installation. In this connection, the coupling of the heat into the saturator cycle, in particular, should not take place directly by means of a medium flowing out of the gasification device or by means of tapped air flowing into the air separation installation. Instead of this, coupling of heat into the saturator cycle is, rather, provided by means of a medium extracted from the water/steam cycle of the steam turbine, it being possible for the operating parameters for the gasification device and/or the air separation installation, on the one hand, and the saturator, on the other, to be set independently of one another. The control devices necessary for operating these components can also, therefore, be comparatively simply constructed.
In a particularly advantageous further development, oxygen from an air separation installation can be supplied to the gasification device, which air separation installation can, for its part, be subjected at the inlet end to a partial flow of air compressed in an air compressor associated with the . gas turbine, a further heat exchanger being connected on the primary side in a tapped air line connecting the air compressor to the air separation installation in order to cool the partial flow of compressed air, the secondary side of which further heat exchanger is connected into a feed water line connecting the saturator-water heat exchanger at the output end to a feed water line associated with the waste-heat steam generator. Such an arrangement ensures a particularly high installation efficiency. The feed water flowing to the saturator-water heat exchanger is initially cooled by the thermal coupling into the water flow guided in the saturator cycle. In the further heat exchanger connected on the feed water side downstream of the saturator-water heat exchanger, the cooled feed water then experiences

7
reheating, cooling, of the partial flow of compressed air, also referred to as tapped air, flowing to the air separation installation, taking place simultaneously. Coupling of heat from the tapped air flow into the water/steam cycle of the steam turbine therefore occurs to provide a particularly large ,

8
recovery of heat.
In order to compensate for losses in the water flow guided in the saturator cycle, for example because of the charging of the gasified fuel with water vapour in the saturator, a feed line expediently opens into the saturator cycle, the entry location of the feed line into the saturator cycle being provided before the saturator-water heat exchanger, viewed in the flow direction of the water flow, in order to provide a particularly high installation efficiency in a particularly advantageous embodiment. With such an arrangement, a particularly high transfer of heat from the feed water to the water flow guided in the saturator cycle is ensured. The feed water therefore flows out of the saturator-water heat exchanger with a particularly low temperature so that, particularly when the cooled feed water is used for cooling the tapped air, a particularly effective cooling of the tapped air is also made possible.
The advantages achieved by the invention consist in particular in the fact that because of the coupling of heat into the saturator cycle by means of feed water extracted from the water/steam cycle of the steam turbine, reliable operation of the saturator is made possible independent of the operating condition of the gasification device. In consequence, the gas turbine in particular can also be operated within specified parameter limits independent of the operating condition of the gasification device. Such a concept for coupling in heat is therefore particularly flexible and, in particular, is. also independent of the integration concept, i.e. independent of the type of air supply for the air separation installation and the components employed for that purpose. Because of the use of the feed water, cooled due to the heat transfer to the water flow, for cooling the tapped air from the air separation installation, a particularly high installation efficiency is also ensured.

9
An embodiment example of the invention is explained in more detail using an accompanying drawing. The figure in the drawing shows, diagrammatically, a gas turbine and steam turbine installation.
The gas turbine and steam turbine installation
1 shown in the figure comprises a gas turbine
installation la and a steam turbine installation lb.
The gas turbine installation la comprises a gas turbine
2 with, connected to it, an air compressor 4 and a
combustion chamber 6, which is connected upstream of
the gas turbine 2 and is connected to a compressed air
line 8 of the compressor 4. The gas turbine 2, the air
compressor 4 and a generator 10 are located on a common
shaft 12.
The steam turbine installation lb comprises a steam turbine 2 0 with, coupled to it, a generator 2 2 and, in a water/steam cycle 24, a condenser 2 6 and a waste-heat steam generator 30 connected downstream of the steam turbine 20. The steam turbine 20 consists of a first pressure stage or a high-pressure part 20a and a second pressure stage or a medium-pressure part 2 0b and a third pressure stage or a low-pressure part 20c, which drive the generator 22 via a common shaft 32.
An exhaust gas line 3 4 is connected to an inlet 3 0a of the waste-heat steam generator 30 in order to feed working medium AM or flue gas expanded in the gas turbine 2 into the waste-heat steam generator 30. The expanded working medium AM from the gas turbine 2 leaves the waste-heat steam generator 3 0 via its outlet 3 0b in the direction of a chimney (not shown in any more detail).
The waste-heat steam generator 3 0 comprises a condensate preheater 40 which can be fed, at its inlet end, with condensate K from the condenser 2 6 via a condensate line 42, into which is connected a condensate pump unit 44. At its outlet end, the condensate preheater 4 0 is connected via a line 45 to a feed water tank 46. In order, if required, to bypass

10
the condensate preheater 40, the condensate line 42 can, in addition, be connected directly to the feed water tank 46 via a bypass line {not shown). The feed water tank 46 is connected via a line 47 to a high-pressure feed pump 48, with medium pressure extraction.
The high-pressure feed pump 48 brings the feed water S flowing from the feed water tank 46 to a pressure level suitable for a high-pressure stage 50 of the water/steam cycle 24 associated with the high-pressure part of the steam turbine 20. The feed water S which is at a high pressure - can be supplied to the high-pressure stage 50 via a feed water preheater 52 which, at its outlet end, is connected to a high-pressure drum 58 via a feed water line 56 which can be shut off by a valve 54. The high-pressure drum 5 8 is connected to a high-pressure evaporator 60 arranged in the waste-heat steam generator 30 for the formation of a water/steam circuit 62. For the removal of the live steam F, the high-pressure drum 58 is connected to a high-pressure superheater 64 arranged in the waste-heat steam generator 30, the high-pressure superheater 64 being connected at its outlet end to the steam inlet 66 of the high-pressure part 20a of the steam turbine 20.
The steam outlet 68 of the high-pressure part 20a of the steam turbine 20 is connected via a reheater 70 to the steam inlet 72 of the medium-pressure part 20b of the steam turbine 20. The steam outlet 74 of the medium-pressure part 20b is connected via a transfer line 76 to the steam inlet 78 of the low-pressure part 20c of the steam turbine 20. The steam outlet 80 of the low-pressure part 20c of the steam turbine 20 is connected via a steam line 82 to the condenser 2 6 so that a closed water/steam cycle 24 results.
In addition, a branch line 84 branches off from the high-pressure feed pump 48 at an extraction location at which the condensate K has reached a medium

11
pressure. This branch line 84 is connected via a further feed water preheater 86 or medium-pressure economizer to a

12
medium-pressure stage 9 0 of the water/steam cycle associated with a medium-pressure part 20b of the steam turbine 20. For this purpose, the second feed water preheater 86 is connected at its outlet end via a feed water line 94, which can be shut off by a valve 92, to a medium-pressure drum 96 of the medium-pressure stage 90. The medium-pressure drum 96 is connected to a heating surface 98 arranged in the waste-heat steam generator 3 0 and configured as a medium-pressure evaporator in order to form a water/steam circuit 100. For the removal of medium-pressure live steam F , the medium-pressure drum 96 is connected via a steam line 102 to the reheater 70 and therefore to the steam inlet 72 of the medium-pressure part 2 0b of the steam turbine 20.
A further line 110, which is provided with a low-pressure feed pump 107, which can be shut off by a valve 108 and which is connected to a low-pressure stage 120 of the water/steam cycle 24 associated with the low-pressure part 20c of the steam turbine 20, branches off from the line 47. The low-pressure stage 12 0 comprises a low-pressure drum 122, which is connected, in order to form a water/steam circuit 12 6, to a heating surface 124 arranged in the waste-heat steam generator 3 0 and configured as a low-pressure evaporator. In order to remove low-pressure live steam F", the low-pressure drum 122 is connected to the transfer line 76 via a steam line 128, into which is connected a low-pressure superheater 129. The water/steam cycle 24 of the gas turbine and steam turbine installation 1 therefore comprises, in the embodiment example, three pressure stages 50, 90, 120. As an alternative, however, fewer pressure stages, in particular two, can be provided.
The gas turbine installation la is configured for operation with a gasified synthesis gas SG which is generated by the gasification of a fossil fuel B. Gasified coal or gasified oil can, for example, be

13
provided as the synthesis gas. For this purpose, the combustion chamber 6 of the gas turbine 2 is connected at its inlet end via a fuel line 130 to a gasification device 132. Coal or oil, as the fossil fuel B, can be supplied to the gasification device 132

14
via a charge system 134.
In order to make available the oxygen 02 necessary for the gasification of the fossil fuel B, an air separation installation 13 8 is connected via an oxygen line 13 6 upstream of the gasification device 132. At its inlet end, the air separation installation 13 8 can be subjected to a partial flow T of the air compressed in the air compressor 4. For this purpose,
the air separation installation 138 is connected, at

its inlet end, to a tapped air line 140 which branches off from the compressed air line 8 at a branch location 142. A further air line 143, into which is connected an additional air compressor 144, also opens into the tapped air line 140. In the embodiment example, the total airflow L flowing to the air separation installation 138 is made up of the partial flow T branched off from the compressed air line 8 and the airflow delivered by the additional air compressor 144. Such a connection concept is also designated a partially integrated installation concept. In an alternative embodiment, the so-called fully integrated installation concept, it is possible to dispense with the further air line 143 and also with the additional air compressor 14 4 so that the complete air feed to the air separation installation 138 takes place by means of the partial flow T extracted from the compressed air line 8.
The nitrogen N2 obtained, in addition to the oxygen O2, in the air separation installation 138 during the separation of the airflow L is supplied to a mixing appliance 146, via a nitrogen line 145 connected to the air separation installation 138, and is there mixed with the synthesis gas SG. The mixing appliance 146 is then configured for a particularly uniform and streak-free mixing of the nitrogen N2 with the synthesis gas SG.
The synthesis gas SG flowing away from the gasification device 132 passes initially, via the fuel line 130, into a

15
crude gas waste-heat steam generator 14 7 in which, by means of heat exchange with a flow medium, cooling of the synthesis gas SG takes place. High-pressure steam generated during this heat exchange is supplied, in a manner not shown in any more detail, to the high-pressure stage 50 of the water/steam cycle 24.
Behind the crude gas waste-heat steam generator 14 7 and before the mixing appliance 14 6, viewed in the flow direction of the synthesis gas SG, a dust-removal device 148 for the synthesis gas SG and a desulphurization installation 149 are connected into the fuel line 130. In an alternative configuration, a soot-washing appliance can also be provided instead of the dust-removal device 148, in particular in the case of the gasification of oil as the fuel.
For particularly low pollutant emission during the combustion of the gasified fuel in the combustion chamber 6, the gasified fuel is charged with water vapour before it enters into the combustion chamber 6. This can take place in a thermally particularly advantageous manner in a saturator system. For this purpose, a saturator 150, in which the gasified fuel is guided in counterflow relative to the heated water flow W (also referred to as saturator water), is connected into the fuel line 13 0. The saturator water or the water flow W then circulates in a saturator cycle 152, which is connected to the saturator 150 and into which a circulating pump 154 is connected. A feed line 158 is connected to the saturator cycle 152 to compensate for losses of saturator water occurring during the saturation of the gasified fuel.
The secondary side of a heat exchanger 159 acting as a crude gas/mixed gas heat exchanger is connected into the fuel line 13 0 behind the saturator 150, viewed in the flow direction of the synthesis gas SG. The primary side of the heat exchanger 159 is then likewise connected into the fuel line 130 at a position

16
in front of the dust removal installation 148, so that the synthesis gas SG flowing to the dust.

17
removal installation 148 transfers a part of its heat to the synthesis gas SG flowing out of the saturator 150. The guidance of the synthesis gas SG via the heat exchanger 159 before it enters the desulphurization installation 149 can then also be provided in a modified connection concept relative to the other components. In the case of the connection of a soot-washing device, in particular, the heat exchanger can preferably be arranged on the crude gas side downstream of the soot-washing device.
The secondary side of a further heat exchanger 160, whose primary side can be heated by feed water or also by steam, is connected into the fuel line 130 between the saturator 150 and the heat exchanger 159. Particularly reliable preheating of the synthesis gas SG flowing to the combustion chamber 6 of the gas turbine 2, even in the case of different operating conditions of the gas turbine and the steam turbine installation 1, is then ensured by the heat exchanger 159, which is configured as a crude gas/clean gas heat exchanger, and by the heat exchanger 160.
In order to subject the synthesis gas SG flowing to the combustion chamber 6 to steam, if required, a further mixing appliance 161 is, in addition, connected into the fuel line 130. Medium-pressure steam can be supplied to this further mixing appliance 161 via a steam line (not shown in any more detail) in order, in particular, to ensure reliable gas turbine operation in the case of operational faults.
In order to cool the partial flow T of compressed air, also designated as tapped air, to be supplied to the air separation installation 13 8, the primary side of a heat exchanger 162 is connected into the tapped air line 140, the secondary side of this heat exchanger 162 being configured as a medium-pressure evaporator for a flow medium S' . The heat exchanger 162 is connected to a water/steam drum 164, which is configured as a medium-pressure drum, in order

18

to form an evaporator circuit 163. The water/steam drum 164 is connected to the medium-pressure drum 96 associated with the water/steam circuit 100

by lines 166, 168. As an alternative, the secondary side of the heat exchanger 162 can also be directly connected to the medium-pressure drum 96. In the embodiment example, the water/steam drum 164 is therefore directly connected to the heating surface 98, which is configured as a medium-pressure evaporator. In addition, a feed water line 170 is connected to the water/steam drum 164 in order to top up evaporated flow medium S'.
A further heat exchanger 172, whose secondary side is configured as the low-pressure evaporator for a flow medium S" is connected into the tapped air line 14 0 after the heat exchanger 162, viewed in the flow direction of the partial flow T of compressed air. The heat exchanger 172 is then connected to a water/steam drum 176, which is configured as a low-pressure drum, in order to form an evaporator circuit 174. In the embodiment example, the water/steam drum 176 is connected to the low-pressure drum 122, which is associated with the water/steam circuit 12 6, via lines 178, 180 and is therefore directly connected to the heating surface 124, which is configured as a low-pressure evaporator. As an alternative, however, the water/steam drum 176 can also be connected in another suitable manner, it being then possible to supply steam taken from the water/steam drum 176 to an auxiliary consumption unit as process steam and/or as steam for heating purposes. In a further alternative embodiment, the secondary side of the heat exchanger 172 can also be directly connected to the low-pressure drum 122. The water/steam drum 176 is, in addition, connected to a feed water line 182.
Each of the evaporator circuits 163, 174 can be configured as a forced circulation system, the circuit of the flow medium S' or S" being ensured by a circulating pump and the flow medium S', S" being at least partially evaporated in a heat exchanger 162 or 172 configured as an evaporator. In the embodiment

20

example, however, both the evaporator circuit 163 and the evaporator circuit 174 are respectively configured as natural circulation systems, the circulation' of the flow medium S' or .

21
S" being ensured by the pressure differences arising during the evaporation process and/or by the geodetic arrangement of the respective heat exchanger 162 or 172

and the respective water/steam drum 164 or 176. In this configuration, only a comparatively modestly dimensioned circulating pump (not shown) is respectively connected into the evaporator circuit 163 or into the evaporator circuit 174 for starting the system.
For the connection of heat into the saturation cycle 152 and therefore for setting a temperature in the water flow W sufficient for charging the synthesis gas SG with water vapour, a saturator-water heat exchanger 184 is provided which can be subjected on the primary side to feed waters from the feed water tank 46. For this purpose, the primary side of the saturator-water heat exchanger 184 is connected/ at the inlet end, via a line 186 to the branch line 84 and, at the outlet end, via a line 188 to the feed water tank 46. The saturator-water heat exchanger 184 is then connected on the secondary side downstream, viewed in the flow direction of the water flow W, of the inlet of the feed line 158 into the saturator cycle 152.
For additional heating of the water flow W, if required, an additional heat exchanger 189 is connected into the saturator cycle 152 in the embodiment example. The additional heat exchanger 189 is then subjected on the primary side to preheated feed water from the medium pressure stage 90 of the water/steam cycle 24. The additional heat exchcinger 18 9 can, however, also be dispensed with - depending on the specified emission figures and/or combustion gas temperatures.
A further heat exchanger 190 is connected into the line 188 for reheating the cooled feed water S flowing from the saturator-water heat exchanger 184, this further heat exchanger 190 being connected on the primary side downstream of the heat exchanger 172 in the tapped air line 140. Such an arrangement can achieve a

22
particularly high heat, recovery from the tapped air and, therefore, a particularly high efficiency of the gas turbine and steam turbine installation 1.
A cooling air line 192, by means of which a partial quantity T' of the cooled partial flow T can be supplied as cooling air to the gas turbine 2 for blade cooling, branches off from the tapped air line 140 between the heat exchanger 172 and the heat exchanger 190, viewed in the flow direction of the partial flow T.
Subjecting the saturator-water heat exchanger 184 to feed water S from the water/steam cycle 24 of the steam turbine 20 permits reliable operation of the saturator 150 independent of the operating condition of the air separation installation 138. The overall efficiency of the gas turbine and steam turbine installation 1 then benefits particularly from the fact that reheating of the feed water S cooled in the saturator-water heat exchanger 184 takes place in the additional heat exchanger 190. This ensures reliable setting of the final temperature of the partial flow T flowing as tapped air to the air separation installation 138 with simultaneous recovery of the heat carried in this for the energy generation process of the gas turbine and steam turbine installation 1.

23 We Claim:
1. A gas and steam turbine plant (1) comprising a waste-heat steam
generator (30) whose flue gas side is connected downstream of a gas
turbine (2), heating surfaces of said waste-heat steam generator (30)
being connected to a water/steam cycle (24) of a steam turbine (20); a
gasification device (132), for fuel (B), connected upstream of a
combustion chamber (6) of the gas turbine (2) by means of a fuel line
(130); a saturator (150), in which the gasified fuel ( SG) being guided
in counterflow to a water flow (W) guided in a saturator cycle (152),
connected into the fuel line ( 130); and a saturator-water heat
exchanger (184) connected on the secondary side into the saturator
cycle (152) to heat the water flow (W), the primary side of said
saturator-water heat exchanger (184) being subjected to feed water (S)
extracted from the water/steam cycle (24) of the steam turbine (20),
the feed water (S) cooled in the saturator-water heat exchanger (184)
being heatable by means of a partial flow (T) of compressed air, the
partial flow (T) of compressed air being supplied to an air separation
installation (138) connected upstream of the gasification device (132),
characterized in that an additional heat exchanger (190) is connected
on the primary side in a tapped air line (140) connecting the air
compressor (4) to the air separation installation (138) in order to cool
the partial flow (T) of compressed air , and in that the secondary side
of the additional heat exchanger (190) is connected into a feed water
line (188) connecting the saturator-water heat exchanger (184) at the
outlet end to a feed water tank (46) associated with the waste-heat
steam generator (30).
2. A gas and steam turbine plant (1) as claimed in claim 1, wherein
oxygen ( O2 ) from the air separation installation (138) supplied to the
gasification device (132), and wherein the air separation installation
(138) is capable of being subjected at the inlet end to the partial flow ( T) of air compressed in an air compressor (4) associated with the gas turbine (2).

24
3. A gas and steam turbine plant (1) as claimed in claim 1 or 2, wherein a feed line (158) opens into the saturator cycle (152) before the saturator-water heat exchanger (184) when viewed in the flow direction of the water flow ( W).
This invention relates to a gas and steam turbine plant (1) comprising a steam generator (30) which uses waste heat and is mounted downstream from the gas turbine (2) on the flue gas side. The heating surfaces of the generator are mounted in the water-steam circuit (24) of said steam turbine (20). A gasification device (132) is mounted downstream from the gas turbine (2) through a fuel duct (130) for integrated gasification of a fossil fuel (B). A saturator (150) is mounted in the fuel duct (130). Reliable operation of said saturator (150) is required for such a gas and steam turbine unit (1) irrespective of the operation mode of said gasification device (132). In addition, a steam water-heat exchanger (184), mounted on the secondary side statutory circuit (132),is fed on its primary side with feeding water (S) drawn from the water steam circuit (24) of the steam turbine (20). The feed water (S) which is cooled in the water-heat exchanger of the saturator (184) can be heated by means of a partial stream (T) of compressed air, whereby said partial stream (T) of compressed air can be transferred to an air separation facility (138) mounted upstream from said gasification device.

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Patent Number

206701

Indian Patent Application Number

IN/PCT/2001/00202/KOL

PG Journal Number

19/2007

Publication Date

11-May-2007

Grant Date

10-May-2007

Date of Filing

19-Feb-2001

Name of Patentee

SIEMENS AKTIENGESELLSCHAFT

Applicant Address

WITTELSBACHERPLATZ 2, D-80333 MUENCHEN

Inventors:

#	Inventor's Name	Inventor's Address
1	SCHIFFERS ULRICH	MORITZBERGSTRASSE 1, D-90542 ECKENTAL
2	HANNEMANN FRANK	HOHE WARTE 2, D-91080 SPARDORT

PCT International Classification Number

F 01 K 23/06

PCT International Application Number

PCT/DE99/02440

PCT International Filing date

1999-08-04

PCT Conventions:

#	PCT Application Number	Date of Convention	Priority Country
1	19837251.5	1998-08-17	Germany