Double-reheat power generator with an ultra high pressure cylinder and a high-intermediate pressure cylinder each having additional heat recovery turbine stages

Abstract

A double-reheat power generator with an ultra high pressure cylinder and a high-intermediate pressure cylinder each having additional heat recovery turbine stages, including steam exhaust of the ultra high pressure cylinder having additional heat recovery turbine stages, that is, first extraction supplies steam to a first high-pressure heater. New second, new third and new fourth extractions of the ultra high pressure cylinder having additional heat recovery turbine stages supply steam to second, third and fourth high-pressure heaters respectively; a new fifth extraction of the HP-IP cylinder having additional heat recovery turbine stages supplies steam to a deaerator; a new sixth extraction of the HP-IP cylinder having additional heat recovery turbine stages supplies steam to an air-preheater; and an air-preheater drainage pump used for water draining of the air-preheater connects to the deaerator.

Claims

1. A double-reheat power generator with an ultra high pressure cylinder and a high-intermediate pressure (HP-IP) cylinder each having additional heat recovery turbine stages, comprising: a boiler water wall and an economizer; a boiler superheater system; the ultra high pressure cylinder having additional heat recovery turbine stages; a boiler primary reheater system; the HP-IP cylinder having additional heat recovery turbine stages; a boiler secondary reheater system; an intermediate-low pressure (IP-LP) cylinder; an air preheater; an air preheater drainage pump; a condenser; a condensate pump; an ultra-low temperature economizer; a deaerator; an electric feedwater pump; a fourth high pressure heater; a third high pressure heater; a second high pressure heater; and a first high pressure heater; wherein the ultra high pressure cylinder having additional heat recovery turbine stages comprises all-pressure-stage impellers, nozzles, steam distribution mechanisms of the ultra high pressure cylinder; a steam exhaust hood of the ultra high pressure cylinder becomes a large extraction steam opening; five short-blade pressure stages are newly added after the steam exhaust hood; and divided steam continues to expand and exert effect in the newly-added pressure stages, and then is output, with a low degree of superheat and a low value of enthalpy, from a new second extraction, a new third extraction and a new fourth extraction, respectively; steam exhaust of the ultra high pressure cylinder having additional heat recovery turbine stages, as a first extraction, supplies steam to the first high pressure heater; the new second extraction of the ultra high pressure cylinder having additional heat recovery turbine stages supplies steam to the second high pressure heater; the new third extraction of the ultra high pressure cylinder having additional heat recovery turbine stages supplies steam to the third high pressure heater; and the new fourth extraction of the ultra high pressure cylinder having additional heat recovery turbine stages supplies steam to the fourth high pressure heater; a new fifth extraction of the HP-IP cylinder having additional heat recovery turbine stages supplies steam to the deaerator; and a new sixth extraction of the HP-IP cylinder having additional heat recovery turbine stages supplies steam to the air preheater; the air preheater drainage pump is configured to pump drainage water of the air preheater to the deaerator; an inlet steam pressure of the ultra high pressure cylinder having additional heat recovery turbine stages is 40 MPa; and an exhaust steam pressure of the ultra high pressure cylinder having additional heat recovery turbine stages is 15 MPa; an inlet steam pressure of the HP-IP cylinder having additional heat recovery turbine stages is 14 MPa; and an exhaust steam pressure of the HP-IP cylinder having additional heat recovery turbine stages is 3.78 MPa; an inlet steam pressure of the IP-LP cylinder is 3.5 MPa; and an exhaust steam pressure of the IP-LP cylinder is 3.5 kPa; a pressure of the new fifth extraction of the HP-IP cylinder having additional heat recovery turbine stages is 1.22 MPa; and a temperature of the new fifth extraction of the HP-IP cylinder having additional heat recovery turbine stages is 255° C.; a pressure of the new sixth extraction of the HP-IP cylinder having additional heat recovery turbine stages is 0.3 MPa; and a temperature of the new sixth extraction of the HP-IP cylinder having additional heat recovery turbine stages is 133.5° C.; and there is a slight humidity; and the air preheater is able to increase an inlet air temperature of an air-heater by 80K to 100 K; and condensate water side outlet design temperature of the ultra-low temperature economizer is 150° C.

2. The double-reheat power generator with the ultra high pressure cylinder and the HP-IP cylinder each having additional heat recovery turbine stages of claim 1, wherein the ultra high pressure cylinder having additional heat recovery turbine stages is single-flow, has tangential full-arc admission, and all consist of impulse turbine stages; a main flow part of the ultra high pressure cylinder having additional heat recovery turbine stages comprises an inner cylinder and an outer cylinder, consists of seven-stage impulse turbine stages or eight-stage impulse turbine stages; the inner cylinder of the ultra high pressure cylinder adopts shrunk-on rings to provide a sealing force of a split face; and the inner cylinder of the ultra high pressure cylinder has a design maximum working pressure of 40 MPa, and does not have a steam extraction port and an overload supplementary steam valve inlet; the additional heat recovery turbine stages that provides the new second extraction, the new third extraction and the new fourth extraction have a single-layer cylinder structure, and consist of a Z1 stage, a Z2 stage, a Z3 stage, a Z4 stage and a Z5 stage; a steam extraction port after the Z1 stage provides the new second extraction; steam extraction ports after the Z2 stage and the Z3 stage provide the new third extraction; and steam extraction ports after the Z4 stage and the Z5 stage provide the new fourth extraction; an amount of extraction steam of the new second extraction matches an amount of condensation steam required by the second high pressure heater; the amount of the condensation steam required by the second high pressure heater is able to heat feedwater flowing through the second high pressure heater to a saturation temperature under a pressure of the second high pressure heater at its shell side; and a pressure of the new second extraction is 105% of the pressure of the second high pressure heater at its shell side; an amount of extraction steam provided by the new third extraction matches an amount of condensation steam required by the third high pressure heater; the amount of the condensation steam required by the third high pressure heater is able to heat feedwater flowing through the third high pressure heater to a saturation temperature under a pressure of the third high pressure heater at its shell side; and a pressure of the new third extraction is 105% of the pressure of the third high pressure heater at its shell side; an amount of extraction steam provided by the new fourth extraction matches an amount of condensation steam required by the fourth high pressure heater; the amount of the condensation steam required by the fourth high pressure heater is able to heat feedwater flowing through the fourth high pressure heater to a saturation temperature under a pressure of the fourth high pressure heater at its shell side; and a pressure of the new fourth extraction is 105% of the pressure of the fourth high pressure heater at its shell side; and an automatic main valve and a speed control valve are arranged on both sides of the ultra high pressure cylinder and are connected to steam inlets on both sides of the ultra high pressure cylinder; and materials of the automatic main valve, the speed control valve, and a rotor, a steam inlet chamber and an inner cylinder of the ultra high pressure cylinder are selected according to a working temperature of 600° C.

3. The double-reheat power generator with the ultra high pressure cylinder and the HP-IP cylinder each having additional heat recovery turbine stages of claim 1, wherein the high-intermediate pressure cylinder having additional heat recovery turbine stages is dual-flow, has tangential full-arc admission, and comprises impulse turbine stages; the high-intermediate pressure cylinder having additional heat recovery turbine stages comprises an inner cylinder and an outer cylinder, consists of 2×7-stage impulse turbine stages or 2×8-stage impulse turbine stages which forms a main flow part of the high-intermediate pressure cylinder without a steam extraction port; the additional heat recovery turbine stages comprising a zz1 stage, a zz2 stage and a zz3 stage are provided on one side of the main flow part; the deaerator is supplied with steam after the zz1 stage; and the air preheater is supplied with steam after the zz3 stage; and steam inlet combined valves of the high-intermediate pressure cylinder are arranged on two sides of the high-intermediate pressure cylinder and are connected to steam inlets on the two sides of the high-intermediate pressure cylinder; and materials of the steam inlet combined valves, and a rotor, an inner cylinder and a steam inlet chamber of the high-intermediate pressure cylinder are selected according to a working temperature of 620° C.

4. The double-reheat power generator with the ultra high pressure cylinder and the HP-IP cylinder each having additional heat recovery turbine stages of claim 1, wherein the intermediate-low pressure cylinder comprises two intermediate-low pressure cylinders, is dual-flow and has four steam exhaust ports; four steam inlet combined valves of the intermediate-low pressure cylinder are divided into two groups, which are arranged on two sides of steam inlet parts of the two intermediate-low pressure cylinders; the intermediate-low pressure cylinder has tangential full-arc admission and comprises an inner layer, a middle layer and an outer layer which forms a three-layered cylinder structure; the intermediate-low pressure cylinder consists of 2×2×8 stage impulse turbine stages without steam extraction ports; the inner layer is a high temperature steam inlet chamber; the middle layer is a low pressure inner cylinder and the outer layer is a low pressure outer cylinder; an outlet of a boiler high temperature secondary reheater is provided with four secondary reheat hot section pipes, which are respectively connected to the four steam inlet combined valves of the intermediate-low pressure cylinder; and materials of the steam inlet combined valves, a rotor, an inner cylinder and a high temperature steam inlet chamber of the intermediate-low pressure cylinder are selected according to a working temperature of 620° C.

5. The double-reheat power generator with the ultra high pressure cylinder and the HP-IP cylinder each having additional heat recovery turbine stages of claim 1, wherein the ultra-low temperature economizer comprises H-shaped fin tubes in series to form a serpentine tube; a base pipe is arranged horizontally; the H-shaped fin tubes are vertically arranged; a low temperature condensate water enters a side of a bottom of the serpentine tube through an inlet header of the ultra-low temperature economizer, and then flows upward along the serpentine pipe; and a flue gas flows from top to bottom to form countercurrent heat transfer; a serpentine group includes several serpentine tubes which are connected in parallel through the inlet header and an outlet header of the ultra-low temperature economizer to form A/B groups of the ultra-low temperature economizer, which are respectively arranged on A/B sides of a low dust flue; through full flow of condensate water, the pressure drop of the ultra-low temperature economizer (12) does not exceed 200 kPa; a countercurrent arrangement is divided into a hot section and a cold section; a part of base tube where a wall temperature thereof is not less than a flue gas acid dew point minus 10K is the hot section that is made of 09CrCuSb (ND steel); and a part of the base tube where the wall temperature thereof is below the flue gas acid dew point minus 10K is the cold section that is made of duplex stainless steel and applied with a polytetrafluoroethylene coating having a thickness of 0.02 mm; and a shell and an expansion joint of the ultra-low temperature economizer are made of ND steel and covered with an anticorrosive layer made of glass fiber reinforced plastics; and a design outlet condensate water temperature of the ultra-low temperature economizer is 150° C., and a design life of the ultra-low temperature economizer is 30 years.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1s a principle thermal system diagram of a double-reheat power generator with an ultra high pressure cylinder and a high-intermediate pressure cylinder each having additional heat recovery turbine stages; in which: 1, boiler water wall and economizer; 2, boiler superheater system; 3, ultra high pressure cylinder having additional heat recovery turbine stages; 4, boiler primary reheating system; 5, high-intermediate pressure cylinder having additional heat recovery turbine stages; 6, boiler secondary reheating system; 7, intermediate-low pressure cylinder; 8, air preheater; 9, air preheater drainage pump; 10, condenser; 11, condensate pump; 12, ultra-low temperature economizer; 13, deaerator; 14, electric feedwater pump; 15, fourth high pressure heater; 16, third high pressure heater; 17, second high pressure heater; and 18, first high pressure heater.

DETAILED DESCRIPTION OF EMBODIMENTS

(2) The present application will be further described below with reference to the drawing to illustrate a preferred embodiment, in which a double-reheat power generator has a 1000 MW grade and design values of main steam temperature/primary reheated steam temperature/secondary reheated steam temperature of turbine sides are respectively 585° C./620° C./620° C.

(3) Provided herein is a double-reheat power generator with an ultra high pressure cylinder and a high-intermediate pressure (HP-IP) cylinder each having additional heat recovery turbine stages, including: a boiler water wall and an economizer (1), a boiler superheater system (2), the ultra high pressure cylinder having additional heat recovery turbine stages (3), a boiler primary reheater system (4), the high-intermediate pressure cylinder having additional heat recovery turbine stages (5), a boiler secondary reheater system (6), an intermediate-low pressure (IP-LP) cylinder (7), an air preheater (8), an air preheater drainage pump (9), a condenser (10), a condensate pump (11), an ultra-low temperature economizer (12), a deaerator (13), an electric feed water pump (14), a fourth high pressure heater (15), a third high pressure heater (16), a second high pressure heater (17) and a first high pressure heater (18).

(4) The ultra high pressure cylinder having additional heat recovery turbine stages (3) includes all-pressure-stage impellers, nozzles, steam distribution mechanisms; a steam exhaust hood of the ultra high pressure cylinder becomes a large extraction steam opening; five short-blade pressure stages are newly added after the steam exhaust hood; divided steam continues to expand and exert effect in the newly-added pressure stages and then is output from a new second extraction port, a new third extraction port and a new fourth extraction port respectively with a low degree of superheat and a low value of enthalpy.

(5) Steam exhaust of the ultra high pressure cylinder having additional heat recovery turbine stages (3), as a first extraction, supplies steam to the first high pressure heater (18); the new second extraction of the ultra high pressure cylinder having additional heat recovery turbine stages (3) supplies steam to the second high pressure heater (17); the new third extraction of the ultra high pressure cylinder having additional heat recovery turbine stages (3) supplies steam to the third high pressure heater (16); and the new fourth extraction of the ultra high pressure cylinder having additional heat recovery turbine stages (3) supplies steam to the fourth high pressure heater (15).

(6) A new fifth extraction of the high-intermediate pressure cylinder having additional heat recovery turbine stages (5) supplies steam to the deaerator (13); and a new sixth extraction of the high-intermediate pressure cylinder having additional heat recovery turbine stages (5) supplies steam to the air preheater (8).

(7) The air preheater drainage pump (9) is configured to pump drainage water of the air preheater (8) to the deaerator (13).

(8) An inlet steam pressure of the ultra high pressure cylinder having additional heat recovery turbine stages (3) is 40 MPa; and an exhaust steam pressure of the ultra high pressure cylinder having additional heat recovery turbine stages (3) is 15 MPa.

(9) An inlet steam pressure of the high-intermediate pressure cylinder having additional heat recovery turbine stages (5) is 14 MPa; and an exhaust steam pressure of the high-intermediate pressure cylinder having additional heat recovery turbine stages (5) is 3.78 MPa.

(10) An inlet steam pressure of the IP-LP cylinder (7) is 3.5 MPa; and an exhaust steam pressure of the IP-LP cylinder (7) is 3.5 kPa.

(11) A pressure of the new fifth extraction of the high-intermediate pressure cylinder having additional heat recovery turbine stages (5) is 1.22 MPa; and a temperature of the new fifth extraction of the high-intermediate pressure cylinder having additional heat recovery turbine stages (5) is 255° C.

(12) A pressure of the new sixth extraction of the high-intermediate pressure cylinder having additional heat recovery turbine stages (5) is 0.3 MPa; a temperature of the new sixth extraction of the high-intermediate pressure cylinder having additional heat recovery turbine stages (5) is 133.5° C.; and there is a slight humidity; the air preheater (8) is able to increase an inlet air temperature of an air-heater by 80K to 100 K; and condensate water side outlet design temperature of the ultra-low temperature economizer (12) is 150° C.

(13) The ultra high pressure cylinder having additional heat recovery turbine stages (3) is single-flow, has tangential full-arc admission, and all consist of impulse turbine stages.

(14) A main flow part of the ultra high pressure cylinder having additional heat recovery turbine stages (3) includes an inner cylinder and an outer cylinder, consists of seven-stage impulse turbine stages or eight-stage impulse turbine stages; the inner cylinder of the ultra high pressure cylinder having additional heat recovery turbine stages (3) adopts shrunk-on rings to provide a sealing force of a split face; and the inner cylinder of the ultra high pressure cylinder having additional heat recovery turbine stages (3) has a design maximum working pressure of 40 MPa, and does not have a steam extraction port and an overload supplementary steam valve inlet.

(15) The additional heat recovery turbine stages that provides the new second extraction, the new third extraction and the new fourth extraction have a single-layer cylinder structure, and consist of a Z1 stage, a Z2 stage, a Z3 stage, a Z4 stage and a Z5 stage; a steam extraction port after the Z1 stage provides the new second extraction; steam extraction ports after the Z2 stage and the Z3 stage provide the new third extraction; and steam extraction ports after the Z4 stage and the Z5 stage provide the new fourth extraction.

(16) An amount of extraction steam of the new second extraction matches an amount of condensation steam required by the second high pressure heater; the amount of the condensation steam required by the second high pressure heater is able to heat feedwater flowing through the second high pressure heater to a saturation temperature under a pressure of the second high pressure heater at its shell side; and a pressure of the new second extraction is 105% of the pressure of the second high pressure heater at its shell side.

(17) An amount of extraction steam provided by the new third extraction matches an amount of condensation steam required by the third high pressure heater; the amount of the condensation steam required by the third high pressure heater is able to heat feedwater flowing through the third high pressure heater to a saturation temperature under a pressure of the third high pressure heater at its shell side; and a pressure of the new third extraction is 105% of the pressure of the third high pressure heater at its shell side;

(18) An amount of extraction steam provided by the new fourth extraction matches an amount of condensation steam required by the fourth high pressure heater; the amount of the condensation steam required by the fourth high pressure heater is able to heat feedwater flowing through the fourth high pressure heater to a saturation temperature under a pressure of the fourth high pressure heater at its shell side; and a pressure of the new fourth extraction is 105% of the pressure of the fourth high pressure heater at its shell side.

(19) An automatic main valve and a speed control valve are arranged on both sides of the ultra high pressure cylinder and are connected to steam inlets on both sides of the ultra high pressure cylinder; and materials of the automatic main valve, the speed control valve, and a rotor, a steam inlet chamber and the inner cylinder of the ultra high pressure cylinder are selected according to a working temperature of 600° C.

(20) The high-intermediate pressure cylinder having additional heat recovery turbine stages (5) is dual-flow, has tangential full-arc admission, and includes impulse turbine stages.

(21) The high-intermediate pressure cylinder having additional heat recovery turbine stages (5) includes an inner cylinder and an outer cylinder, consists of 2×7-stage impulse turbine stages or 2×8-stage impulse turbine stages which forms a main flow part of the high-intermediate pressure cylinder without a steam extraction port; the additional heat recovery turbine stages including a zz1 stage, a zz2 stage and a zz3 stage are provided on one side of the main flow part; the deaerator (13) is supplied with steam after the zz1 stage; and the air preheater (8) is supplied with steam after the zz3 stage.

(22) Steam inlet combined valves of the high-intermediate pressure cylinder are arranged on two sides of the high-intermediate pressure cylinder and are connected directly to steam inlets on the two sides of the high-intermediate pressure cylinder; and materials of the steam inlet combined valves, and the rotor, the inner cylinder and the steam inlet chamber of the high-intermediate pressure cylinder are selected according to a working temperature of 620° C.

(23) The intermediate-low pressure cylinder (7) includes two intermediate-low pressure cylinders, is dual-flow and has four steam exhaust ports; four steam inlet combined valves of the intermediate-low pressure cylinder are divided into two groups, which are arranged on two sides of steam inlet parts of the two intermediate-low pressure cylinders; the intermediate-low pressure cylinder (7) has tangential full-arc admission and includes an inner layer, a middle layer and an outer layer which forms a three-layered cylinder structure; the intermediate-low pressure cylinder consists of 2×2×8 stage impulse turbine stages without steam extraction ports; the inner layer is a high temperature steam inlet chamber; the middle layer is a low pressure inner cylinder and the outer layer is a low pressure outer cylinder; an outlet of a boiler high temperature secondary reheater is provided with four secondary reheat hot section pipes, which are respectively connected to the four steam inlet combined valves of the intermediate-low pressure cylinder; and materials of the steam inlet combined valves, the rotor, the inner cylinder and the high temperature steam inlet chamber of the intermediate-low pressure cylinder are selected according to a working temperature of 620° C.

(24) The ultra-low temperature economizer (12) includes H-shaped fin tubes in series to form a serpentine tube; a base pipe is arranged horizontally; the H-shaped fin tubes are vertically arranged; a low temperature condensate water enters a side of a bottom of the serpentine tube through an inlet header of the ultra-low temperature economizer (12), and then flows upward along the serpentine pipe; and a flue gas flows from top to bottom to form countercurrent heat transfer.

(25) A serpentine group includes several serpentine tubes which are connected in parallel through the inlet header and an outlet header of the ultra-low temperature economizer (12) to form A/B groups of the ultra-low temperature economizer (12), which are respectively arranged on A/B sides of a low dust flue.

(26) Through full flow of condensate water, the pressure drop of the ultra-low temperature economizer (12) does not exceed 200 kPa; a countercurrent arrangement is divided into a hot section and a cold section; a part of base tube where a wall temperature thereof is not less than a flue gas acid dew point minus 10K is the hot section that is made of 09CrCuSb (ND steel); a part of the base tube where the wall temperature thereof is below the flue gas acid dew point minus 10K is the cold section that is made of duplex stainless steel and applied with a polytetrafluoroethylene coating having a thickness of 0.02 mm.

(27) A shell and an expansion joint of the ultra-low temperature economizer (12) are made of ND steel and covered with an anticorrosive layer made of glass fiber reinforced plastics; and a design outlet condensate water temperature of the ultra-low temperature economizer (12) is 150° C., and a design life of the ultra-low temperature economizer (12) is 30 years.