U.S. patent application number 09/758186 was filed with the patent office on 2001-10-18 for process for the recovery of water from the flue gas of a combined cycle power station, and combined cycle power station for performing the process.
Invention is credited to Bachmann, Rolf.
Application Number | 20010029732 09/758186 |
Document ID | / |
Family ID | 7627367 |
Filed Date | 2001-10-18 |
United States Patent
Application |
20010029732 |
Kind Code |
A1 |
Bachmann, Rolf |
October 18, 2001 |
Process for the recovery of water from the flue gas of a combined
cycle power station, and combined cycle power station for
performing the process
Abstract
In a process for the recovery of water, which arises from the
combustion of a fuel (19), particularly natural gas, in a combined
cycle power station (101) comprising a gas turbine plant (11), a
waste heat boiler (33), and a steam turbine (25) arranged in a
water/steam circuit with the waste heat boiler (33), and/or which
is added in the form of water or steam (36), the water is condensed
out from the flue gas (42) arising from the combustion of the fuel
(19) and containing water in the form of water vapor after flowing
through the waste heat boiler (33), and is separated in liquid
form, in particular by expansion in a utilization turbine (20).
Inventors: |
Bachmann, Rolf; (Dottingen,
CH) |
Correspondence
Address: |
Robert S. Swecker
BURNS, DOANE, SWECKER & MATHIS, L.L.P.
P.O. Box 1404
Alexandria
VA
22313-1404
US
|
Family ID: |
7627367 |
Appl. No.: |
09/758186 |
Filed: |
April 12, 2001 |
Current U.S.
Class: |
60/772 ;
60/39.182 |
Current CPC
Class: |
B01D 53/002 20130101;
B01D 5/0039 20130101; Y02E 20/14 20130101 |
Class at
Publication: |
60/39.02 ;
60/39.182 |
International
Class: |
F02C 006/18 |
Foreign Application Data
Date |
Code |
Application Number |
Jan 13, 2000 |
DE |
100 01 110.1 |
Claims
1. Process for the recovery of water which arises in a combined
cycle power station (10; 101, . . . ,103) comprising a gas turbine
plant (11), a waste heat boiler (33), and a steam turbine (25)
arranged in a water/steam circuit with the waste heat boiler (33),
during the combustion of fuel (19), in particular natural gas,
and/or is added in the form of water or steam (36), wherein the
water is condensed out and is separated in liquid form from the
flue gas (42) arising from the combustion of the fuel (19) and
containing water in the form of water vapor, after passage through
the waste heat boiler (33).
2. Process according to claim 1, wherein the flue gas (42) is
expanded to condense the water out, with an output of work.
3. Process according to claim 2, wherein the expansion is carried
out by means of a utilization turbine (20).
4. Process according to one of claims 2 and 3, wherein the waste
heat boiler (33) is operated with respect to the flue gas (42) at a
pressure exceeding the ambient air pressure by a few bar,
preferably 2-5 bar, and wherein the flue gas (42) is brought to
ambient air pressure by the subsequent expansion.
5. Process according to one of claims 2 and 3, wherein the waste
heat boiler (33) is operated with respect to the flue gas (42) at
about ambient air pressure, the flue gas (42) is subsequently
expanded in a vacuum, and the flue gas (43) after water removal is
compressed again to ambient air pressure.
6. Process according to one of claims 2-5, wherein the water is
separated from the flue gas (42) during the expansion or in the
utilization turbine (20) itself.
7. Process according to one of claims 2-5, wherein the water is
separated from the flue gas (42) in one of the expansion or the
droplet separator (23) which follows the utilization turbine
(20).
8. Process according to claim 1, wherein the waste heat boiler (33)
is operated with respect to the flue gas (42) at a pressure
exceeding the ambient air pressure by in particular a few bar,
preferably 2-5 bar; that the water is condensed out of the flue gas
(42) after leaving the waste heat boiler on cold surfaces, in
particular, the cold tubes of a heat exchanger (45), and that the
dewatered flue gas (43) is brought to ambient air pressure by a
subsequent expansion.
9. Process according to claim 8, wherein the expansion is carried
out by means of a utilization turbine (20).
10. Combined cycle power station (10, . . . ,103) for carrying out
the process according to claim 1, which combined cycle power
station (101 . . . ,103) comprises a gas turbine plant (11) with a
combustion chamber (15) for the combustion of the fuel (19), a
waste heat boiler (33) connected to the gas turbine plant (11) for
the production of steam by means of the hot flue gases (42) of the
gas turbine plant (11), and a steam turbine (25) arranged together
with the waste heat boiler (33) in a water/steam circuit, wherein
means (20, 23, 44, 45) for the condensation of water vapor
contained in the flue gas (42) and separation of the condensed
water follow the waste heat boiler (33).
11. Combined cycle power station according to claim 10, wherein the
condensation and separation means comprise means for the expansion
of the flue gas (42), preferably in the form of a utilization
turbine (18, 20).
12. Combined cycle power station according to claim 11, wherein a
droplet separator (23) follows the expansion means or the
utilization turbine (18, 20).
13. Combined cycle power station according to claim 11, wherein the
expansion means comprises a utilization turbine (18) expanding into
vacuum, and wherein a compressor (44) follows the utilization
turbine (18).
14. Combined cycle power station according to claim 11, wherein
condensation means, in particular in the form of a heat exchanger
(45), are arranged between the waste heat boiler (33) and the
expansion means or the utilization turbine (20).
Description
FIELD OF TECHNOLOGY
[0001] The present invention relates to the field of combined cycle
power stations (combined plant). It relates to a process according
to the preamble of claim 1 and also to a combined cycle power
station for carrying out the process according to the preamble of
claim 10.
STATE OF THE ART
[0002] Combined cycle power stations normally burn natural gas,
which produces water vapor during combustion. 1 kg of natural gas
burns to about 2 kg of water and also CO.sub.2. The flue gas with
the water contained therein is usually discharged through a chimney
at elevated temperatures, without the water being used to
advantage. The same also holds for water or steam, which in other
cases is injected or sprayed in during combustion and thus becomes
a component of the flue gas. On the other hand, water already forms
an increasingly valuable resource at the present time.
[0003] The simplified diagram of an exemplary combined cycle power
station from the state of the art is reproduced in FIG. 1. The
combined cycle power station 10 essentially comprises a gas turbine
plant 11, a waste heat boiler (heat recovery steam generator HRSG)
33, and a steam turbine 25, which are connected together. The gas
turbine plant 11 consists of a compressor 14 and a turbine 17,
which are arranged on a rotor 16, and also a combustion chamber 15.
In operation, the compressor 14 sucks in air through an air inlet
12, compresses it, and delivers the compressed air to the
combustion chamber 15, where it enters combustion as combustion
air, together with a liquid or gaseous fuel 19 (e.g., natural gas)
which is fed in through a fuel supply duct 21. In addition, water
or steam 36 can be injected or sprayed into the combustion chamber
15 to reduce the combustion temperature. The hot combustion gases
are conducted from the combustion chamber 15 into the turbine 17,
where they set the rotor 16 in rotation. The flue gas 42 exiting
the turbine 17 is then conducted through the waste heat boiler 33
for the production of steam, where it flows in succession through a
superheater 40, an evaporator 39, and a preheater (economizer) 34,
and gives up heat stepwise. The cooled flue gas 42 finally leaves
the waste heat boiler 33 and is usually, possibly after a flue gas
cleaning, discharged from a chimney.
[0004] The superheater 40, evaporator 39 and preheater 34 are
connected in series as part of a water/steam circuit, in which the
steam turbine is also connected. The exhaust steam from the steam
turbine 25 passes into a condenser 26 and condenses there. The
condensate is pumped by a condensate pump 28, possibly with the
addition of additional water 27, through a feed water duct 29 to a
feed water container 30 with degasser. The degassed condensate is
then pumped as feed water 32 through the preheater 34 by a boiler
feed pump 31, and as pressurized feed water 35 to a steam drum 37
with the connected evaporator 39. The steam then passes to the
superheater 40, where it is superheated, and finally drives the
steam turbine 25 as superheated steam 41. Both the steam turbine 25
and also the gas turbine plant 11 respectively drive a generator 13
or 24 which produces electrical current. Means for the recovery of
water or water vapor contained in the flue gas are not provided
here.
DESCRIPTION OF THE INVENTION
[0005] The invention therefore has as its object to provide a
process and also a combined cycle power station with which the
water contained in the flue gas is recovered and can be
advantageously reused.
[0006] The object is attained by means of the entirety of the
features of claims 1 and 10. The core of the invention consists of
configuring the combined cycle power station and conducting the
process so that the water is condensed out of the flue gas after
leaving the waste heat boiler and is separated in liquid form.
[0007] A first preferred embodiment of the process according to the
invention is characterized in that the flue gas is expanded for
condensing the water out, with output of work. The expansion is
preferably carried out by means of a utilization turbine. In
particular, the waste heat boiler is operated for this purpose at a
pressure exceeding the ambient air pressure by several bar,
preferably 2-5 bar, and the flue gas is brought to the ambient air
pressure by the subsequent expansion. Alternatively to this, the
waste heat boiler can be operated at about the ambient pressure
with respect to the flue gas, the flue gas subsequently being
expanded into a vacuum, and the flue gas being compressed again to
ambient air pressure after the separation of water. In both cases,
the water is separated from the flue gas particularly during the
expansion or in the utilization turbine itself, and/or in a droplet
separator following the expansion or the utilization turbine.
[0008] A second preferred embodiment of the process according to
the invention is characterized in that the waste heat boiler is
operated with respect to the flue gas at a pressure exceeding the
ambient air pressure by several bar, preferably 2-5 bar, in that
the water is condensed out of the flue gas on cold surfaces after
leaving the waste heat boiler, in particular on the cold tubes of a
heat exchanger, and in that the dewatered flue gas is brought to
the ambient air pressure by a subsequent expansion; here also, the
expansion is preferably carried out by means of a utilization
turbine.
[0009] A preferred embodiment of the combined cycle power station
according to the invention is distinguished in that the means for
condensation and separation comprise means for the expansion of the
flue gas, preferably in the form of a utilization turbine.
[0010] A first development of this embodiment is characterized in
that the expansion means or the utilization turbine is followed by
a droplet separator.
[0011] A second development of this embodiment is characterized in
that the expansion means comprises a utilization turbine working in
vacuum, and that a compressor follows the utilization turbine.
[0012] A third development of this embodiment is characterized in
that condensation means, particularly in the form of a heat
exchanger, is arranged between the waste heat boiler and the
expansion means.
BRIEF DESCRIPTION OF THE DRAWINGS
[0013] The invention will be explained in detail hereinafter using
embodiment examples in combination with the accompanying
drawings.
[0014] FIG. 1 is a simplified diagram of an exemplary combined
cycle power station from the state of the art, to which the
invention can be applied;
[0015] FIG. 2 is a T-S [temperature-entropy] diagram illustrating
the conduct of the process in a preferred embodiment example of the
process according to the invention;
[0016] FIG. 3 is a diagram of a combined cycle power station
comparable to FIG. 1, according to a first embodiment example of
the invention, with an expansion of the flue gas to ambient air
pressure;
[0017] FIG. 4 is a diagram of a combined cycle power station
comparable to FIG. 1, according to a second embodiment example of
the invention, with an expansion of the flue gas into vacuum and
subsequent compression to ambient air pressure;
[0018] FIG. 5 is a diagram of a combined cycle power station
comparable to FIG. 1, according to a third embodiment example of
the invention, with an expansion of the flue gas to ambient air
pressure after a preceding condensation of the water vapor.
PREFERRED EMBODIMENTS OF THE INVENTION
[0019] The basic idea of the invention can be characterized as
"supercharged waste heat boiler of a combined cycle power station
with water separation by way of temperature drop or partial
pressure". The idea can be explained using the T-S diagram shown in
FIG. 2 of an example of the performance of the process. From the
point P1 on the isobar of the ambient air pressure p.sub.A, the air
sucked in by the compressor (14 in FIG. 1) is compressed along the
curve a to the combustion chamber pressure (isobar P.sub.BK) and is
heated in the combustion chamber at constant pressure (curve b).
The gas turbine (17 in FIG. 1) in a combined plant now expands the
flue gas along the curve c to a pressure p.sub.K in the waste heat
boiler (33 in FIG. 1), which is at several bar, e.g., 2-5 bar,
above the ambient air pressure p.sub.A. The "supercharged" waste
heat boiler removes heat from the flue gas for the production of
steam, and thus cools the flue gas to about 80-90.degree. C. (curve
d).
[0020] If now this flue gas is expanded (along the curve e) by
means of a utilization turbine or comparable means, low
temperatures arise at the point P2 after the turbine, corresponding
to the pressure before the turbine. The water content of the flue
gas condenses, particles which may be present in the flue gas serve
as condensation nuclei. The water can then be separated in the
turbine itself or in a subsequent droplet separator, and
subsequently drawn off.
[0021] A combined cycle power station 101 designed for the
performance of this process is reproduced in FIG. 3, which is
comparable to the illustration of FIG. 1 (the same parts are given
the same reference numerals). The combined cycle power station 101
of FIG. 3 differs from the combined cycle power station 10 of FIG.
1 in the flue gas sequence following the waste heat boiler 33. In
the combined cycle power station 101, a utilization turbine 20
(which for example drives a generator 22) for the exiting flue gas
42 containing water vapor, and also a droplet separator 23, follow
the waste heat boiler 33. The flue gas 42 under pressure is cooled
in the utilization turbine 20 by expansion. The water vapor then
condenses and can be removed either already at the utilization
turbine 20 or in the following droplet separator 23. The
"dewatered" flue gas 43 then leaves the droplet separator 23. This
kind of water recovery has the following advantages:
[0022] The plant is very compact; the gas turbine can, e.g., be
embodied as a variant of a standard machine without end stage;
[0023] good heat transfer coefficients are obtained in the waste
heat boiler;
[0024] a chimney can be omitted, since the "dewatered" flue gas
leaves the plant at low temperatures;
[0025] the "cold" of the flue gases can be further utilized, e.g.,
for cooling purposes or at the intake side of the gas turbine
(booster).
[0026] On the other hand, a slight performance loss results, since
the expansion line of the gas turbine is made smaller, and this is
only partially compensated by the recuperation in the steam turbine
and in the utilization turbine after the waste heat boiler. In
order to remedy it, the water recovery can also be carried out in a
modified form:
[0027] In an alternative manner of conducting the process, for
which the combined cycle power station 102 according to FIG. 4 is
designed, the waste heat boiler 33 is not "supercharged", but
operates at about atmospheric pressure. The following utilization
turbine 18 (with generator 22) expands the flue gas 42 into a
vacuum. After the separation of the water (H2O) in the utilization
turbine 18 or in a following droplet separator 23, the "dewatered"
flue gas 43 is again compressed to ambient air pressure in a
compressor 44 (with a reduced flue gas mass flow).
[0028] In another alternative manner of conducting the process, for
which the combined cycle power station 103 according to FIG. 5 is
designed, the waste heat boiler 33--as in the combined cycle power
station 101 of FIG. 3--is run "supercharged". After leaving the
waste heat boiler, the water vapor of the flue gas 42 is condensed
on cold surfaces or tubes of a heat exchanger 45, making use of the
high partial pressure. An expansion of the "dewatered" flue gas 43
takes place thereafter in a utilization turbine 20.
1 List of Reference Numbers 10, 101-103 combined cycle power
station 11 gas turbine plant 12 air inlet 13, 22, 24 generator 14
compressor 15 combustion chamber 16 rotor 17 turbine 18, 20
utilization turbine 19 fuel 21 fuel supply duct 23 droplet
separator 25 steam turbine 26 condenser 27 additional water 28
condensate pump 29 feed water duct 30 feed water container 31
boiler feed pump 32 feed water 33 waste heat boiler (HRSG) 34
preheater 35 pressurized feed water 36 water or steam 37 steam drum
38 saturated steam 39 evaporator 40 superheater 41 superheated
steam 42 flue gas (water vapor containing) 43 flue gas (dewatered)
44 compressor 45 heat exchanger P.sub.A ambient air pressure
P.sub.BK combustion chamber pressure P.sub.K boiler pressure P1, P2
point a-e curves
* * * * *