U.S. patent number 3,776,164 [Application Number 05/185,597] was granted by the patent office on 1973-12-04 for apparatus for filling and, if desired, emptying inert gas poor in oxygen into or from holds in ships, respectively.
This patent grant is currently assigned to A/S Kongsberg Vapenfabrikk. Invention is credited to Thorbjorn Westrum.
United States Patent |
3,776,164 |
Westrum |
December 4, 1973 |
APPARATUS FOR FILLING AND, IF DESIRED, EMPTYING INERT GAS POOR IN
OXYGEN INTO OR FROM HOLDS IN SHIPS, RESPECTIVELY
Abstract
Exhaust gases from an emergency or auxilliary gas
turbine/generator set are passed to an afterburner in which the
rather high oxygen content of said exhaust gases is reduced to an
acceptable level for use of the resulting gas as an inert
explosion-proof gas for empty oil tanks. Before the gas is supplied
to the tanks it is cooled by water supplied by a pump driven by the
electric current produced by the generator. No blowers are
required, since the turbine may operate against the pressure
required for feeding the gas through the afterburner and the cooler
and into the tanks. For displacing the inert gas from the tanks
when desired, compressed air from the compressor unit of the
turbine/generator set is tapped off and passed through an injector
in which additional air from the atmosphere is entrained. The
combined air is passed through the cooler and fed to the tanks
through a suitable distribution system.
Inventors: |
Westrum; Thorbjorn (Kongsberg,
NO) |
Assignee: |
A/S Kongsberg Vapenfabrikk
(Konsberg, NO)
|
Family
ID: |
19879823 |
Appl.
No.: |
05/185,597 |
Filed: |
October 1, 1971 |
Foreign Application Priority Data
Current U.S.
Class: |
440/89R; 422/612;
440/89B; 60/276; 422/198 |
Current CPC
Class: |
B01J
19/14 (20130101); B63B 57/04 (20130101); A62C
99/0018 (20130101); A62C 3/10 (20130101) |
Current International
Class: |
B01J
19/14 (20060101); B63B 57/00 (20060101); B63B
57/04 (20060101); B63b 017/00 () |
Field of
Search: |
;23/281
;60/39.5,39.07,276,39.02 ;123/136 ;114/.5 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Halvosa; George E. A.
Assistant Examiner: Goldstein; Stuart M.
Claims
What I claim is
1. Apparatus for filling and, if desired, emptying inert gas, poor
in oxygen, into or from holds in ships, respectively, said
apparatus being connected to the exhaust conduit from a gas
turbine, said apparatus comprising an afterburner for reduction of
the oxygen content of the exhaust gases of the turbine, a cooler
for reduction of the temperature of the gases, a discharge conduit
for the cooled combustion gases and a valve for controlling the
supply of exhaust gases to maintain the pressure of the inert gas
within the desired limits.
2. Apparatus as claimed in claim 1, characterized by an oxygen
analyser for analysing the oxygen content of the supplied inert gas
and a valve for controlling the supply of fuel to the afterburner
said valve being controlled in accordance with the result of the
analysis.
3. Apparatus as claimed in claim 2, characterized by a branch
conduit leading from the discharge conduit for inert gas into the
atmosphere and one or more valves controlled by the oxygen analyser
for supplying gas to the branch conduit instead of the discharge
conduit when the oxygen content is not within the prescribed
limits.
4. Apparatus as claimed in claim 3, characterized by an air conduit
for connection to the pressure side of the compressor unit of the
turbine and delivery of compressed air to the discharge conduit
through the cooler and an injector inserted in said air conduit and
operated by the compressed air from the compressor to draw
additional air into the air conduit.
Description
BACKGROUND OF THE INVENTION
The present invention relates to a method and an apparatus for
filling and, if desired, emptying inert gas, poor in oxygen, into
or from holds or rooms in ships, respectively, in which method and
apparatus combustion gases are produced in a combustion device,
which gases are cooled and supplied to the holds to be filled.
A number of serious explosion accidents in tankers have proved that
it is important to control the gas content of ships' tanks so that
the gas mixture is explosion-proof. Plants or apparatus have
therefore been developed, in which the exhaust gases from the
burners serving for the production of steam for the main engine
and/or auxilliary engines of the ship are supplied to the tanks of
the ship as the tanks are emptied of oil. Such an apparatus has the
advantage that the costs thereof are moderate, and that it has a
relatively low power demand (for the operation of a blower
supplying the exhaust gases to the tanks with the desired
overpressure). However, such apparatus also have several
disadvantages. Firstly, the oxygen content of the exhaust gases
varies considerably. The apparatus further depends upon the steam
boilers being in operation and upon the operating condition of the
boilers. The exhaust gases entrain impurities and cause deposits on
the blowers, valves and conduits. Sulphuric or sulphurous acid may
be present in the exhaust gases, and the required blower is
seriously exposed to corrosion. Therefore, the apparatus requires a
rather large amount of maintenance. In addition, the blower
required for blowing the exhaust gases into the tanks of the ship
produce rather much noise.
Further, the system depends upon the presence of a burner for a
steam boiler.
There have also been developed plants or apparatus working with
separate gas generators, i.e. burners especially adapted for the
production of an inert gas, poor in oxygen, for use in ships'
tanks. Such apparatus produce a very pure gas with low oxygen and
sulphur contents and is, of course, independent of a firing of
steam boilers. The disadvantages of such an apparatus are that it
is extremely expensive and has a very large power demand and fuel
consumption.
SUMMARY OF THE INVENTION
The object of the present invention is to provide a method and an
apparatus of the kind initially referred to, which does neither
depend on steam boiler burners nor require any blower for providing
the required pressure of the inert gases, but is still
substantially cheaper than an apparatus having a separate gas
generator. The inert gas is primarily intended for the filling of
empty oil tanks, but may also be used for instance in extinguishing
fire in engine rooms.
The method of the invention is characterized in that as a
combustion device there is used a gas turbine which also serves
other purposes, for instance the operation of a generator, the
exhaust gases of the turbine being supplied to an afterburner for
reduction of the oxygen content of the gases and then to the
desired holds by the pressure downstream of the turbine and without
the aid of blowers.
The apparatus of the invention is primarily characterized in that
it is adapted to be connected to the exhaust conduit from a gas
turbine which also serves other purposes, for instance the
operation of a generator, said apparatus comprising an afterburner
for reduction of the oxygen content of the exhaust gases, a cooler
for reduction of the temperature of the gases, a discharge conduit
for the cooled combustion gases and a valve for controlling the
supply of exhaust gases to maintain the pressure of the inert gas
within the desired limits.
Gas turbines are often installed as an auxilliary or emergency set
onboard ships. Such sets are mostly not in use when the ship is
unloading, and the set is then available for the production of
inert gas for the filling of the oil tanks of the ship as these
tanks are emptied. It is true that the exhaust gases from a gas
turbine are not directly suited as an inert gas for said purpose,
since the oxygen content is comparatively high. However, the oxygen
content is relatively constant, and the exhaust gases therefore
lend themselves to an afterburning for reduction of the oxygen
content. The essential advantage in using a gas turbine for
producing the desired inert gases is primarily that no blower
whatsoever is required, since the turbine may supply the exhaust
gases at the pressure required for introducing the gases into tanks
and other holds or rooms in the ship. Such a back-pressure
downstream of the turbine will of course reduce the output of the
turbine. However, the remaining output will be sufficient not only
for operating a cooling water pump for cooling the exhaust gases,
but also for supplying electric current to the electric
distribution network of the ship during the unloading period. As an
example, it may be mentioned that a gas turbine which normally
delivers 1,100 to 1,200 kW to the network will still deliver about
600 kW to the network when the back-pressure is increased from 14.2
psia (1 atmosphere) to about 18.5 psia. Approximately half of said
output is required for the operation of the cooling water pump, but
there still remains a net output of approximately 300 kW.
Another essential advantage of the combination of an inert gas
apparatus with a gas turbine is that thereby a simple possibility
is provided for removing the inert gas from the holds of the ship
when this is required. Thus, according to the invention, air having
the required pressure for displacing the inert gas from the holds
of the ship may be supplied from the compressor unit of the gas
turbine, a portion of the air compressed in the compressor being
passed through an injector in which the pressure is reduced and
additional air is drawn in. Air of suitable pressure supplied from
the injector is passed through the cooler of the apparatus to
reduce the temperature of the air and further to the tanks in order
to displace the inert gas therein. In the apparatus of the
invention this possibility is provided for by the fact that the
apparatus comprises an air conduit for connection to the pressure
side of the compressor unit of the turbine and delivery of
compressed air to the discharge conduit through the cooler and an
injector inserted in said air conduit and operated by the
compressed air from the compressor to draw additional air into the
air conduit.
Further features of the invention will appear from the following
description of an embodiment, reference being had to the
accompanying drawing, which illustrates the operating principles of
an apparatus according to the invention.
DETAILED DESCRIPTION OF THE DRAWING
In the drawing, the elements included in a conventional auxilliary
and/or emergency set driven by a gas turbine are indicated within a
frame G shown by a dot-and-dash-line. These elements consist of the
gas turbine itself, which in the drawing has been divided into its
three functional units, viz. a compressor 1, a combustion chamber 2
and a turbine 3. The generator is indicated at 4, whereas 5 is an
oil tank for operation of the gas turbine, the oil being supplied
to the combustion chamber 2 of the gas turbine set by a pump 6. The
exhaust gases from the gas turbine are ordinarily let out into the
atmosphere through an exhaust conduit 7 and an exhaust pipe 8
within the ship's funnel.
The inert gas apparatus according to the invention is based upon
the presence of such a gas turbine set and is connected to this set
in the following way:
An exhaust conduit 9 is connected to the exhaust conduit 7. The
distribution of the exhaust gases on the exhaust pipe 8 and the
exhaust conduit 9 is controlled by a throttle valve 10 in the
exhaust pipe 8 in a manner which will be described later in more
detail. When the inert gas apparatus is not in operation, the
exhaust conduit 9 is closed by a valve 11.
The exhaust gases from the exhaust conduit 9 are passed to an
afterburner 12 having a fuel nozzle 13 fed from the fuel tank 5
through a conduit 14 by means of a pump 15. The fuel amount is
controlled in a manner which will be described later in more
detail.
The afterburner is required primarily to reduce the oxygen content
of the exhaust gases from the gas turbine. Typically, such exhaust
gases from the gas turbine may have the following analysis:
percent by volume:
Co.sub.2 -- 3.25
h.sub.2 0 -- 2.32
so.sub.2 -- 0.0056
o.sub.2 -- 16.1
n.sub.2 -- 77.8
downstream of the afterburner the exhaust gases may have the
following composition:
percent by volume:
Co.sub.2 -- 15
co -- 0.1
h.sub.2 -- 0.1
o.sub.2 -- about 1
N.sub.2 -- 83.8
the exhaust gases from the afterburner 12 are passed into a cooling
tower 16 in which they are cooled by spraying with sea water
supplied through a conduit 17 by means of a cooling water pump 18.
The cooling water collects in the bottom of the cooler 16 and is
discharged into the sea through a conduit 19.
The cooled gases are passed through a water separator 20 and
further through a discharge conduit 21 leading to a distributing
system not shown.
A pressure indicator 22 measures the pressure in the discharge
conduit 21, and a feedback 23 actuating the throttle valve 10 in
the exhaust pipe 8 controls the pressure in the discharge conduit
21 so as to maintain the pressure constant at the desired value,
which may for instance be 16.4 psia.
To the discharge conduit 21 there is further connected an oxygen
analyser 24. This analyser actuates a valve 25 in a return conduit
26 for the fuel supplied by the pump 15. When the oxygen content in
the discharge conduit 21 is excessive, the flow of fuel through the
valve 25 is further throttled, whereby more fuel will be supplied
to the afterburner 12 through the fuel nozzle 13. If the oxygen
content in the exhaust gases lies below a certain limit, this must
be taken as an indication that an incomplete combustion may take
place in the afterburner 12, and that the exhaust gases may contain
an excessive amount of carbon monoxide. The flow through the valve
25 will then be increased so that the fuel supply to the fuel
nozzle 13 is reduced.
The oxygen analyser 24 also actuates a valve 27 in the discharge
conduit 21 and a valve 28 in a conduit 29 branched from the
discharge conduit 21 and leading to the atmosphere. The valves 27
and 28 are so controlled that the exhaust gases are passed to the
ship's holds through the distribution system not shown, only when
the oxygen content lies within predetermined limits, whereas the
gases are passed to the atmosphere through the conduit 21 when the
oxygen content is too high or too low, a low oxygen content being,
as already mentioned, interpreted as an indication of an excessive
carbonmonoxide content. 34 is a safety valve.
When the apparatus according to the invention is to be used for
displacing the inert gas from the holds in the ship by means of
fresh air having the required pressure, the valve 11 will be closed
and the afterburner 12 and the described control devices will be
out of operation. A portion of the air compressed by the compressor
1 is diverted through a conduit 30. This, of course, reduces the
output of the gas turbine 3, and it must be expected that the
generator 4 cannot be subjected to a load during this period. The
compressed air from the conduit 30 is supplied to an injector 31
which reduces the pressure of the air and at the same time draws in
additional air through an air inlet 32. From a gas turbine set of
the capacity previously referred to it is possible to tap off about
9,000 standard m.sup.3 air per hour at a pressure of approximately
37 psia. A corresponding amount of air may be drawn into the
injector so that in the conduit 33 from the injector 31 there may
flow about 18,000 standard m.sup.3 air per hour having a pressure
of about 18.5 psia. The temperature of the air tapped from the
compressor is about 170.degree. C. This temperature is reduced in
the injector partly because of the expansion and partly because of
admixture with air drawn in through the air inlet 32. The air in
the conduit 33 will therefore have a temperature of about
100.degree. C. For further cooling this air is passed into the
cooler 16 and further through the discharge conduit 21 into the
distribution system (not shown) for fresh air.
A gas turbine set of the capacity previously referred to will
produce about 31,000 standard m.sup. 3 exhaust gas per hour, and
when the pressure in the exhaust conduit downstream of the turbine
is to be 18.5 psia, the temperature of the exhaust gases will be
about 550.degree. C. The exhaust temperature will of course rise
further in the after-burner, and when the apparatus is to supply
inert gas, comparatively large amounts of cooling water (about
1,500 m.sup. 3 per hour) will be required in the cooler 12. As
previously indicated the pump 18 for circulating this amount of
cooling water may be operated with an input of about 300 kW, which
may be provided by the gas turbine set. When the set supplies air
for displacing the inert gas from the tanks, a substantially lower
amount of cooling water is required, since in this case only about
18,000 standard m.sup.3 air per hour must be cooled from a
temperature of about 100.degree. C.
* * * * *