Technical field
[0001] The present invention relates to a marine vessel waste treatment installation, which
installation includes at least one waste receiving unit, at least one waste feeding
unit, at least one incinerator unit provided with an outlet, and at least one flue
gas pipeline connected to the outlet, which marine vessel waste treatment installation
includes an inline cooling arrangement, which includes a water injection device with
a water discharge nozzle for feeding a water stream directly into the flue gas pipeline
at a given location of the flue gas pipeline and a pressurized air injection device
for feeding pressurized air into the water stream, whereby the pressurized air injection
device is connected to the water injection device so that it is arranged to feed pressurized
air into the water stream before it is discharged from the water discharge nozzle,
and which flue gas pipeline is provided with a temperature measuring unit, the water
injection device is provided with a flow control means for adjusting a flow volume
of the water stream based on a temperature measured by the temperature measuring unit
and the pressurized air feed device is provided with a pressure control means for
adjusting a pressure of the pressurized air based on a temperature measured by the
temperature measuring unit, according to the pre-characterizing portion of claim 1.
The present invention also relates to a method for flue gas cooling in a marine vessel
waste treatment installation according to the pre-characterizing portion of claim
3.
Background art
[0002] Various waste treatment installations are known from prior art. Typical waste treatment
installations, also for treating wet waste such as food waste and so-called household
waste, include a waste feeding hopper, from which waste is fed onto a transport screw
which forwards the waste into an incinerator furnace. Burning of the waste takes place
in the incinerator furnace e.g. at a temperature of 850 °C to 1200 °C. An example
of such an installation is known from
EP 1 384 948 B1.
[0003] In such known waste treatment installations flue gas resulting from the burning of
the waste has a very high temperature which generates dioxin-like chemicals.
[0004] In order to reduce the amount of generated dioxin-like chemicals a number of different
solutions have been presented.
CN 102230627 discusses a land based refuse combustion furnace with a separate gas quenching cooling
tower. The cooling tower is provided with cooling water atomizers in order to lower
the temperature of the flue gas.
CN 103644570 discloses another known land based solution where high pressure water mist is used
for quenching flue gas in connection with the combustion furnace. These are technically
complex and space requiring constructions.
EP 1 065 444 B1 discloses other exhaust gas cooling arrangements where high pressure water and high
pressure air is introduced into a separate cooling chamber through a separate mixing
device or high pressure hot water is introduced to an exhaust gas duct.
[0005] Further,
US 2006/0166152 A1 discloses a gas incinerator device for burning primarily boil-off gas on board a
liquified gas tanker. The gas incinerator device is supplied with additional combustion
air as well as separately delivered outside air flow and water for cooling combusted
gas.
US 2004/0262787 A1 discloses a gas conditioning unit for an industrial plant in which a gas cooling/conditioning
tower is provided with a pressurized air-water spray for conditioning the gas in the
conditioning tower.
JP 2001 269530 A discloses another solution where gas is treated in a cooling tower by a pressurized
air-water spray in order to avoid corrosion of the cooling tower.
[0007] These are technically complex constructions making them very expensive and apt to
functional failure. Furthermore, the known solutions are space demanding making them
unsuitable for marine vessels.
Summary of invention
[0008] An object of the present invention is to avoid the drawbacks of prior art and to
achieve an efficient marine vessel waste treatment installation with a simple flue
gas cooling arrangement fulfilling the requirements of the relevant IMO Resolutions.
This object is attained by a marine vessel waste treatment installation according
to claim 1 and a method for flue gas cooling in a marine vessel waste treatment installation
according to claim 3.
[0009] The basic idea of the present invention is to effectively cool the flue gas within
a short distance after the flue gas enters the flue gas pipeline from the outlet of
the incinerator unit. This is achieved by an inline cooling arrangement that is installed
in the flue gas pipeline. The cooling arrangement includes a water injection device
with a water discharge nozzle for feeding a water stream directly into the flue gas
pipeline at a given location of the flue gas pipeline. The cooling arrangement further
includes a pressurized air injection device for feeding pressurized air into the water
stream.
[0010] The advantage of the present invention is that no auxiliary cooling reactor is required.
In addition, it is only necessary to provide the flue gas pipeline with a technically
simple cooling arrangement and a temperature measuring arrangement. This is a technically
advantageous and inexpensive measure, which requires no extra space onboard the marine
vessel.
[0011] The pressurized air fed into the water stream disperses the water into mist that
has a maximal surface to cool the flue gas within a given distance of about 2.5 m
in the flue gas pipeline measured from the outlet of the incinerator unit. The flue
gas is cooled to a temperature under or about 250 °C.
[0012] This particular requirement is based on the IMO Resolution MEPC 244(66), the Standard
Specification for Shipboard Incinerators.
[0013] A further advantageous feature of the marine waste treatment installation is given
in claim 2.
Brief description of drawings
[0014] In the following the invention will be described, by way of example only, with reference
to the accompanying schematic drawings, in which
Figs. 1 and 2 show a first arrangement,
Figs. 3 and 4 show a preferred embodiment of the present invention, and
Figs. 5 and 6 show a second arrangement.
Detailed description
[0015] In figures 1 to 6 a marine vessel V waste treatment installation is indicated by
reference numeral 1. The waste treatment installation 1 is installed on board a marine
vessel V as indicated in Figures 1, 3 and 5.
[0016] The waste treated onboard the marine vessel V waste treatment installation 1 is normally
composed of a mixture of dry waste and wet waste. Typically dry waste according to
IMO standards would be composed of about 40% of cardboard, 30 % of other packaging
and paper, 20% of fibers and 10% of plastics. Typically wet waste would be composed
of food waste and sludge with a maximum moisture content of about 80%. The purpose
is to maintain average moisture content of the waste mixture at a level of about 50%
or below in order to ensure that the waste mixture burns efficiently in an incinerator
unit.
[0017] Figures 1 and 2 illustrate a first arrangement, figures 3 and 4 illustrate a preferred
embodiment of the present invention, and figures 5 and 6 illustrate a second arrangement.
Generally these comprise similar arrangements, whereby the main difference is in a
cooling arrangement provided for the waste treatment installation, which is described
separately in more detail below.
[0018] The main components of the waste treatment installation 1 include a waste receiving
unit 2, a waste feeding unit 3, and an incinerator unit 4. Flue gas resulting from
the burning of the waste in the incinerator unit 4 is discharged into a flue gas pipeline
8 from an outlet 7 of the incinerator unit 4. The flue gas pipeline 8 is directly
connected to the outlet 7 of the incinerator unit 4.
[0019] The incinerator unit 4 may include a secondary burning chamber 6 with a flue gas
channel 5 arranged before the actual outlet 7 of the incinerator unit 4. The waste
mixture is burned in the incinerator unit 4 where after the flue gases resulting from
the burning of the waste or waste mixture are discharged through the outlet 7 into
the flue gas pipeline 8. In case the incinerator unit 4 includes a secondary burning
chamber 6, an additional burning phase can take place in the secondary burning chamber
6 to ensure high fly-ash separation and a more complete burning of the flue gases.
Such an arrangement would provide for a long gas retention time resulting in very
clean burning. The first section of the incinerator unit 4 and the secondary burning
chamber 6 are advantageously connected by the flue gas channel 5. The flue gas pipeline
8 is advantageously provided with a blower 9 in order to enhance the efficiency of
discharge of the flue gas.
[0020] In order to effectively cool the flue gas in the flue gas pipeline 8, the marine
vessel V waste treatment installation 1 includes an inline cooling arrangement 10
connected to the flue gas pipeline 8. The inline cooling arrangement 10 includes a
water injection device 11 with a water discharge nozzle 12 for feeding a water stream
directly into the flue gas pipeline 8 at a given location A of the flue gas pipeline
8. The water injection device 11 is directly connected to and installed in a casing
81 of the flue gas pipeline 8 so that the water discharge nozzle 12 is located inside
the casing 81, whereby the water can be fed directly into the flue gas discharged
into and flowing in the flue gas pipeline 8.
[0021] The water injection device 11 receives line pressure water from a source of water
13 onboard the marine vessel V, the line pressure usually being approximately 4 bar,
normally available on a marine vessel. Between the water injection device 11 and the
source of water 13 there is a flow control means 14 for adjusting and controlling
the volume of water flow.
[0022] Further, the cooling arrangement 10 is provided with a pressurized air injection
device 16 for feeding pressurized air into the water stream as the water is discharged
from the water discharge nozzle 12 (Figures 1 and 2), into the water as it flows through
the water injection device (Figures 3 and 4), or into the water after it is discharged
from the water discharge nozzle 12 (Figures 5 and 6).
[0023] Pressurized air is provided to the pressurized air injection device 16 from a source
of pressurized air 17 onboard the marine vessel V. Between the source of pressurized
air 17 and the pressurized air injection device 16 there is a pressure control unit
18. The pressurized air used in this cooling arrangement is the pressurized air normally
available in machinery rooms on a marine vessel.
[0024] The flue gas pipeline 8 is provided with a temperature measuring unit 20 at a given
distance D from the outlet 7 of the incinerator unit 4. The given distance is under
or about 2.5 m as discussed above. The volume of water flow is controlled and adjusted
based on the temperature measured by the temperature measuring unit 20 as indicated
by broken lines in Figures 1-6. The pressure of the pressurized air is controlled
and adjusted based on the temperature measured by the temperature measuring unit 20
as indicated by broken lines in Figures 1-6. By optimizing the volume of water flow
and the pressure of the pressurized air the desired degree of cooling can be achieved,
i.e. a flue gas temperature of under or about 250 °C in the flue gas pipeline 8 at
the given distance of about 2.5 m from the outlet 7 of the incinerator unit 4.
[0025] In the arrangement of Figures 1 and 2, the water injection device 11 is provided
with a channel for the water stream coming from the source of water 13 and a surrounding
double hollow jacket. The pressurized air injection device 16 is directly connected
to the interior of the hollow jacket of the water injection device 11 from the side
of the water injection device 11 so that pressurized air is fed into and along the
hollow jacket and into the water discharge nozzle 12, whereby pressurized air is introduced
into the water discharge nozzle 12 so that the pressurized air encounters the water
stream as it is discharged from the water discharge nozzle 12 into the flue gas flowing
in the flue gas pipeline 8. The pressurized air could also be fed to the water discharge
nozzle 12 e.g. through a separate tubing.
[0026] In the preferred embodiment of Figures 3 and 4, the water injection device 11 is
provided with a channel for the water stream coming from the source of water 13 and
a surrounding jacket. The pressurized air injection device 16 leads directly into
the water channel through the jacket from the side of the water injection device 11,
whereby the pressurized air is introduced into the water stream already as it flows
along the water channel and before the water is discharged from the water discharge
nozzle 12 into the flue gas flowing in the flue gas pipeline 8.
[0027] In the arrangement of Figures 5 and 6, the water injection device 11 is provided
with a channel for the water stream coming from the source of water 13 and a surrounding
jacket. In this embodiment, the pressurized air injection device 16 is directly connected
to and installed in the casing 81 of the flue gas pipeline 8, separately from the
water injection device 11, so that the pressurized air injection device 16 is partly
located inside the casing 8. The pressurized air injection device 16 is installed
closely to the discharge nozzle 12 of the water injection device 11. In this way,
the pressurized air is fed directly into water after the water is discharged from
the water discharge nozzle 12 into the flue gas flowing in the flue gas pipeline 8.
[0028] In all three, the pressurized air fed into the water stream disperses the water into
mist that has a maximal surface to cool the flue gas within the given distance of
about 2.5 m in the flue gas pipeline measured from the outlet 7 of the incinerator
unit 4. The flue gas is cooled to a temperature about or under 250 °C.
[0029] The drawings and the description related thereto are only intended for clarification
of the basic idea of the invention. The invention may vary in detail within the scope
of the ensuing claims.
1. A marine vessel (V) waste treatment installation (1), which includes at least one
waste receiving unit (2), at least one waste feeding unit (3), at least one incinerator
unit (4) provided with an outlet (7), and at least one flue gas pipeline (8) connected
to the outlet (7), which marine vessel (V) waste treatment installation includes an
inline cooling arrangement (10), which includes a water injection device (11) with
a water discharge nozzle (12) for feeding a water stream directly into the flue gas
pipeline (8) at a given location (A) of the flue gas pipeline (8) and a pressurized
air injection device (16) for feeding pressurized air into the water stream, whereby
the pressurized air injection device (16) is connected to the water injection device
(11) so that it is arranged to feed pressurized air into the water stream before it
is discharged from the water discharge nozzle (12), and which flue gas pipeline (8)
is provided with a temperature measuring unit (20), the water injection device (11)
is provided with a flow control means (14) for adjusting a flow volume of the water
stream based on a temperature measured by the temperature measuring unit (20) and
the pressurized air injection device (16) is provided with a pressure control means
(18) for adjusting a pressure of the pressurized air based on a temperature measured
by the temperature measuring unit (20), wherein the flue gas pipeline (8) is directly
connected to the outlet (7) of the incinerator unit (4), the temperature measurement
unit (20) is located in the flue gas pipeline (8) within a given distance (D) of 2.5
m from the outlet (7) of the incinerator unit (4), and wherein the flue gas is arranged
to be cooled to a give temperature of 250°C or under at said given distance (D) from
the outlet (7).
2. A marine vessel (V) waste treatment installation according to claim 1, wherein the
water injection device (11) is directly connected to and installed in a casing (81)
of the flue gas pipeline (8).
3. A method for flue gas cooling in a marine vessel (V) waste treatment installation
(1), which installation includes at least one waste receiving unit (2), at least one
waste feeding unit (3), at least one incinerator unit (4) provided with an outlet
(7), and at least one flue gas pipeline (8) connected to the outlet (7), in which
method the flue gas is discharged into the flue gas pipeline (8), in which method
the flue gas in the flue gas pipeline (8) is cooled by means of an inline cooling
arrangement (10), by which inline cooling arrangement a water stream is fed directly
into the flue gas pipeline (8) through a water discharge nozzle (12) at a given location
(A) of the flue gas pipeline (8) and by which inline cooling arrangement pressurized
air is fed into the water stream before it is discharged from the water discharge
nozzle (12), the temperature of the flue gas in the flue gas pipeline (8) is measured,
a flow volume of the water stream is adjusted based on the measured temperature of
the flue gas and a pressure of the pressurized air is adjusted based on the measured
temperature of the flue gas, wherein according to the method the flue gas pipeline
(8) is directly connected to the outlet (7) of the incinerator unit (4), the temperature
is measured in the flue gas pipeline (8) within a given distance (D) of 2.5 m from
the outlet (7) of the incinerator unit (4), and wherein the flue gas is cooled to
a given temperature of 250°C or under at the time it reaches said given distance (D)
from the outlet (7).
1. Abfallbehandlungsanlage (1) für Wasserfahrzeuge (V), die mindestens eine Abfallaufnahmeeinheit
(2), mindestens eine Abfallzuführeinheit (3), mindestens eine Verbrennungseinheit
(4), die mit einem Auslass (7) versehen ist, und mindestens eine Rauchgasleitung (8),
die mit dem Auslass (7) verbunden ist, umfasst, wobei die Abfallbehandlungsanlage
für Wasserfahrzeuge (V) eine Inline-Kühlanordnung (10) umfasst, die eine Wassereinspritzvorrichtung
(11) mit einer Wasserausstoßdüse (12) zum Einspeisen eines Wasserstroms an einer gegebenen
Stelle (A) der Rauchgasleitung (8) direkt in die Rauchgasleitung (8) und eine Drucklufteinspritzvorrichtung
(16) zum Einspeisen von Druckluft in den Wasserstrom umfasst, wobei die Drucklufteinspritzvorrichtung
(16) mit der Wassereinspritzvorrichtung (11) so verbunden ist, dass sie dafür ausgelegt
ist, Druckluft in den Wasserstrom einzuspeisen, bevor dieser von der Wasserausstoßdüse
(12) abgegeben wird, und wobei die Rauchgasleitung (8) mit einer Temperaturmesseinheit
(20) versehen ist, die Wassereinspritzvorrichtung (11) mit einem Durchflusssteuerungsmittel
(14) zum Anpassen einer Durchflussmenge basierend auf einer durch die Temperaturmesseinheit
(20) gemessenen Temperatur versehen ist und die Drucklufteinspritzvorrichtung (16)
mit einem Drucksteuerungsmittel (18) zum Anpassen eines Drucks der Druckluft basierend
auf einer durch die Temperaturmesseinheit (20) gemessenen Temperatur versehen ist,
wobei die Rauchgasleitung (8) direkt mit dem Auslass (7) der Verbrennungseinheit (4)
verbunden ist, die Temperaturmesseinheit (20) in der Rauchgasleitung (8) innerhalb
eines gegebenen Abstands (D) von 2,5 m vom Auslass (7) der Verbrennungseinheit (4)
angeordnet ist, und wobei das Rauchgas dafür ausgelegt ist, in dem gegebenen Abstand
(D) vom Auslass (7) auf eine gegebene Temperatur von 250 °C oder niedriger gekühlt
zu werden.
2. Abfallbehandlungsanlage für Wasserfahrzeuge (V) nach Anspruch 1, wobei die Wassereinspritzvorrichtung
(11) direkt mit einem Gehäuse (81) der Rauchgasleitung (8) verbunden und in diesem
installiert ist.
3. Verfahren zur Rauchgaskühlung in einer Abfallbehandlungsanlage (1) für Wasserfahrzeuge
(V), wobei die Anlage mindestens eine Abfallaufnahmeeinheit (2), mindestens eine Abfallzuführeinheit
(3), mindestens eine Verbrennungseinheit (4), die mit einem Auslass (7) versehen ist,
und mindestens eine Rauchgasleitung (8), die mit dem Auslass (7) verbunden ist, umfasst,
wobei das Rauchgas in dem Verfahren in die Rauchgasleitung (8) abgegeben wird, wobei
das Rauchgas in der Rauchgasleitung (8) in dem Verfahren mittels einer Inline-Kühlanordnung
(10) gekühlt wird, wobei ein Wasserstrom durch die Inline-Kühlanordnung durch eine
Wasserausstoßdüse (12) an einer gegebenen Stelle (A) der Rauchgasleitung (8) direkt
in die Rauchgasleitung (8) eingespeist wird, und wobei Druckluft durch die Inline-Kühlanordnung
in den Wasserstrom eingespeist wird, bevor dieser aus der Wasserausstoßdüse 12) abgegeben
wird, die Temperatur des Rauchgases in der Rauchgasleitung (8) gemessen wird, eine
Durchflussmenge des Wasserstroms basierend auf der gemessenen Temperatur des Rauchgases
angepasst wird und ein Druck der Druckluft basierend auf der gemessenen Temperatur
des Rauchgases angepasst wird, wobei, gemäß dem Verfahren, die Rauchgasleitung (8)
direkt mit dem Auslass (7) der Verbrennungseinheit (4) verbunden ist, die Temperatur
in der Rauchgasleitung (8) innerhalb eines gegebenen Abstands (D) von 2,5 m von dem
Auslass (7) der Verbrennungseinheit (4) gemessen wird, und wobei das Rauchgas zu dem
Zeitpunkt, zu dem es den gegebenen Abstand (D) vom Auslass (7) erreicht, auf eine
gegebene Temperatur von 250 °C oder niedriger gekühlt wird.
1. Installation de traitement de déchets (1) d'un navire (V), comprenant au moins une
unité de réception de déchets (2), au moins une unité d'alimentation en déchets (3),
au moins une unité d'incinérateur (4) dotée d'une sortie (7), et au moins une conduite
de gaz de combustion (8) reliée à la sortie (7), ladite installation de traitement
de déchets d'un navire (V) comprenant un système de refroidissement en ligne (10)
comprenant un dispositif d'injection d'eau (11) avec une buse de décharge d'eau (12)
destinée à introduire un jet d'eau directement dans la conduite de gaz de combustion
(8) à un endroit donné (A) de la conduite de gaz de combustion (8) et un dispositif
d'injection d'air comprimé (16) destinée à introduire de l'air comprimé dans le jet
d'eau, moyennant quoi le dispositif d'injection d'air comprimé (16) est relié au dispositif
d'injection d'eau (11) de manière à pouvoir introduire de l'air comprimé dans le jet
d'eau avant qu'il ne soit déchargé à partir de la buse de décharge d'eau (12), et
ladite conduite de gaz de combustion (8) étant dotée d'une unité de mesure de la température
(20), le dispositif d'injection d'eau (11) étant doté d'un moyen de régulation de
flux (14) permettant de régler un débit du jet d'eau sur la base d'une température
mesurée par l'unité de mesure de la température (20) et le dispositif d'injection
d'air comprimé (16) étant doté d'un moyen de régulation de la pression (18) destiné
à régler une pression de l'air comprimé sur la base d'une température mesurée par
l'unité de mesure de la température (20), dans laquelle la conduite de gaz de combustion
(8) est reliée directement à la sortie (7) de l'unité d'incinérateur (4), l'unité
de mesure de la température (20) se trouve dans la conduite de gaz de combustion (8)
à une distance donnée (D) de 2,5 m de la sortie (7) de l'unité d'incinérateur (4),
et dans laquelle
le gaz de combustion est destiné à être refroidi à une température donnée de 250°
ou moins à ladite distance donnée (D) de la sortie (7).
2. Installation de traitement de déchets d'un navire (V) selon la revendication 1, dans
laquelle le dispositif d'injection d'eau (11) est relié directement à une gaine (81)
de la conduite de gaz de combustion (8) et installé dans celle-ci.
3. Procédé pour le refroidissement de gaz de combustion dans une installation de traitement
de déchets (1) d'un navire (V), ladite installation comprenant au moins une unité
de réception de déchets (2), au moins une unité d'alimentation en déchets (3), au
moins une unité d'incinérateur (4) dotée d'une sortie (7), et au moins une conduite
de gaz de combustion (8) reliée à la sortie (7), ledit procédé comprenant la décharge
du gaz de combustion dans la conduite de gaz de combustion (8), ledit procédé comprenant
le refroidissement du gaz de combustion dans la conduite de gaz de combustion (8)
à l'aide d'un système de refroidissement en ligne (10), ledit système de refroidissement
en ligne permettant d'introduire un jet d'eau directement dans la conduite de gaz
de combustion (8) à travers une buse décharge d'eau (12) à un endroit donné (A) de
la conduite de gaz de combustion (8) et ledit système de refroidissement en ligne
permettant d'introduire de l'air comprimé dans le jet d'eau avant qu'il ne soit déchargé
à partir de la buse décharge d'eau (12), la température du gaz de combustion dans
la conduite de gaz de combustion (8) étant mesurée, un débit du jet d'eau étant réglé
sur la base de la température mesurée du gaz de combustion et une pression de l'air
comprimé étant réglée sur la base de la température mesurée du gaz de combustion,
dans lequel selon le procédé, la conduite de gaz de combustion (8) est reliée directement
à la sortie (7) de l'unité d'incinérateur (4), la température est mesurée dans la
conduite de gaz de combustion (8) à une distance donnée (D) de 2,5 m de la sortie
(7) de l'unité d'incinérateur (4), et dans lequel le gaz de combustion est refroidi
à une température donnée de 250°C ou moins au moment où il a parcouru ladite distance
donnée (D) à partir de la sortie (7).