TECHNICAL FIELD
[0001] The present disclosure relates to a circuit breaker with metallic enclosure as set
forth in the claims. It further relates to a method of manufacturing a circuit breaker
with metallic enclosure.
BACKGROUND OF THE DISCLOSURE
[0002] Circuit breakers with metallic enclosures generally comprise a chamber connected
to the phase and a tank or enclosure enclosing the chamber. Commonly, the tank is
electrically connected to the ground and provides a hermetically closed vessel to
contain the insulating gas. The chamber is subdivided into two compartments which
are electrically insulated from each other. Each compartment is connected to a power
line. A switching actuator is provided to selectively make electric contact between
the compartments or to open the contact so as to selectively close and open a circuit
between the two power lines. The tank is filled with a dielectric gas to cool and
quench an arc occurring when switching the circuit. Moreover, unwanted discharge over
gaps between components shall be avoided. A gas commonly used in current circuit breaker
with metallic enclosures is sulphur hexafluoride, due to the high dielectric withstand.
On the other hand, leaking sulphur hexafluoride yields undesirable environmental impacts.
[0003] When the switching actuator opens or closes the circuit, a temporary arc occurs inside
the chamber. This arc heats the gas inside the chamber. In embodiments of circuit
breaker with metallic enclosures a flow path is provided between the interior of the
chamber and an exterior volume between a wall of the tank and the chamber. It has
been observed, however, that the hot gases exiting the chamber essentially displace
the colder gas in the exterior volume. Mixing between the hot and the colder gases
is very poor. Plumes and strains of hot gases thus become present in the space between
the chamber and the tank. Those yield a lower dielectric withstand than the colder
gas, which increases the propensity for spark-over between the chamber and the tank.
Moreover, the hot gas strains or plumes may become present in the space between the
chamber and the tank at the time when the peak transient recovery voltage appears
after switching. Accordingly, the distance between the tank and the chamber must be
sufficiently large to avoid spark-over to the tank even when adverse effects accumulate.
[0004] If it is desired to replace sulphur hexafluoride with other gases which inhibit less
environmental hazard, the issue gets even more accentuated. Carbon dioxide, for an
instance, already yields a lower dielectric momentum. On top, it has a lower molecular
weight and lower heat capacity. Thus, the temperature increase due to the energy intake
from the switching arc is increased, resulting in an even more fierce discharge of
heated gas into the space between the chamber and the tank. As a result, the already
lower dielectric withstand, when compared to sulphur hexafluoride, is even further
reduced, and the chance of hot gas being present at critical locations upon the occurrence
of the peak transient recovery voltage is increased. Consequently, under the circumstances
outlined, safety against spark-over between the chamber and the tank requires an increase
in size. This in turn adds cost, weight, and increases the space requirement.
OUTLINE OF THE SUBJECT MATTER OF THE PRESENT DISCLOSURE
[0005] The present disclosure is related to a circuit breaker with metallic enclosure of
the type initially mentioned. In an aspect, the safety and/or the margin against spark-over
between the chamber and the tank shall be increased. In aspects, it shall be possible
to replace sulphur hexafluoride as the dielectric gas by an environmentally less hazardous
gas, without increasing the physical dimensions of the circuit breaker, or, in other
aspects, to limit the increase in physical dimensions due to the gas replacement.
Said replacement gas may comprise, while not being limited to, carbon dioxide; wherein
the carbon dioxide may or may not be combined with dioxide, i.e. molecular O
2, and/or nitrogen, and/or an organofluorine compound selected from the group of a
fluoronitrile, a fluoroketone, a fluoroolefine, a fluoroether, an oxirane, a fluoroamine
and mixtures and/or by-products of said gases, and further including mixtures of said
organofluorine compound with carbon dioxide, ; wherein the carbon dioxide further
may or may not be combined with dioxide, i.e. molecular O
2, and/or nitrogen. In another aspect, a circuit breaker with metallic enclosure shall
be provided which can be built, independently from the dielectric gas used, as small
as possible while providing a sufficient margin against spark-over between the chamber
and the tank at a given rated voltage.
[0006] This is achieved by the subject matter described in claim 1.
[0007] Accordingly, disclosed is a circuit breaker with metallic enclosure comprising a
chamber. The circuit breaker may in instances be one of dead tank switchgear and a
gas insulated switchgear. The chamber comprises a first compartment and a second compartment
each having an interior volume, wherein the first and second compartments are electrically
insulated from each other. A switching actuator is displaceably provided inside at
least one of the compartments and configured and adapted to selectively provide electric
connection between the compartments. A sealed tank, which constitutes the enclosure
enclosing the circuit breaker, encloses the chamber. The tank is electrically insulated
from the chamber, whereby an exterior volume is provided between a wall of the tank
and the chamber. Each of the compartments is connected to a line connector penetrating
the tank. The penetration opening of each line connector through the tank is sealed.
The line connectors are electrically insulated from the tank. The tank and the compartments
contain a dielectric gas. The interior of each compartment of the chamber is fluidly
connected to the exterior volume by a flow path having an overall flow cross section.
The flow path between the interior volume of each of the compartments and the exterior
volume is subdivided into a multitude of ducts, each duct having a partial flow cross
section, a hydraulic diameter and a length, wherein the length of each duct is at
least twice the hydraulic diameter of the duct. In exemplary embodiments, the length
of each duct is at least five times the hydraulic diameter of the duct. In even more
specific exemplary embodiments the length of each duct is at least ten times the hydraulic
diameter of the duct. In certain embodiments the length of each duct may be one of
the aforementioned minimum values or more and 100 or less times the hydraulic diameter
of the duct.
[0008] Subdividing the ducts into a multitude of smaller ducts having a relatively long
length compared to the flow cross section yields various advantages. On the one hand,
a gas blow of heated gas exiting the chamber resulting from an arc inside the chamber
has a large contact surface with solid material while escaping from the compartment
into the exterior volume, which in turn results in a reduction of the temperature
of the escaping gas. The comparatively large gas path length results of a delay of
the heated gas exiting into the exterior volume. The heated gas may thus be discharged
into the exterior volume only well after the appearance of the peak transient recovery
voltage, that is, after the appearance of the peak voltage between the terminals after
current interruption. This yields in a lower risk of spark-over between the terminals
and spark-over to the tank between the chamber and the tank. An improved mixing between
the hot gas emanating from the interior of the chamber and the colder gas in the exterior
volume may be achieved, which in turn would yield an improved dielectric withstand
of the gas in the exterior volume, again yielding a reduced propensity for spark-over
to the tank. Moreover, the reduced gas velocity at the exit into the exterior volume
results in reducing the appearance of streaks of unmixed hat gas in the exterior volume,
which additionally supports reducing the propensity for spark-over to the tank.
[0009] The synthesis of these benefits allows to use dielectric gases having a lower molecular
weight, dielectric withstand and thermal capacity than the quite commonly and widely
used sulphur hexafluoride, without the need to increase for instance the distance
between the chamber and the tank. Such dimensional increase is highly undesirable
as it negatively impacts space requirements, weight and cost. For instance, carbon
dioxide may be used to replace sulphur hexafluoride as the dielectric gas inside the
tank, despite the fact is has been shown to increase the transient recovery voltage
and, by virtue of the lower molecular weight and heat capacity, experiences a larger
temperature increase by the switching arc. On the upside, however, the potential environmental
impact of carbon dioxide or the above mentioned organofluorine compounds, also in
mixture with carbon dioxide, is significantly lower than that of sulphur hexafluoride.
[0010] It might also be possible, alternatively or in addition to expanding the choice of
suitable dielectric gases, to reduce the overall dimensions of the circuit breakers,
resulting in benefits as to the space requirements, weight and cost.
[0011] Further effects and advantages of the disclosed subject matter, whether explicitly
mentioned or not, will become apparent in view of the disclosure provided below.
[0012] It is noted that within the framework of the present disclosure the use of the indefinite
article "a" or "an" does in no way stipulate a singularity nor does it exclude the
presence of a multitude of the named member or feature. It is thus to be read in the
sense of "at least one" or "one or a multitude of".
[0013] It may be provided that the chamber comprises two compartments which are coaxially
arranged adjacent each other. Each compartment may, under these circumstances, have
a free axial end on which the ducts for providing fluid communication between the
interior volume of the respective compartment and the exterior volume is provided.
The switching actuator may be a rod with a longitudinal axis extending parallel to
the axes of the compartments. The rod may be arranged coaxially with the compartments.
The rod may be contained inside at least one of the compartments and may be axially
displaceable along a longitudinal axis of the rod or the axes of the compartments,
respectively.
[0014] In more specific embodiments of the herein disclosed circuit breaker with metallic
enclosure at least one duct extends from an inlet adjacent the interior volume of
a compartment to an outlet adjacent the exterior volume, wherein further a lateral
fluid connection between the duct and the exterior volume is provided and joins the
duct between the inlet and the outlet. While hot gases flow through the duct from
inside the chamber, or compartment, respectively, colder gas from the exterior volume
may thus be entrained through the lateral fluid connection. This embodiment fosters
a mixing of the hot gas flowing from inside the chamber, or compartment, respectively,
with colder gas from the exterior volume, resulting in a temperature reduction of
the gases discharged through the duct and into the exterior volume. Thus, any strains
or bubbles of discharged gas eventually forming in the exterior volume will be less
prone to cause spark-over to the tank as the detrimental effect on the dielectric
withstand is reduced. This may be achieved in that, in embodiments, at least one duct
comprises a lateral opening in the duct wall.
[0015] In embodiments, the fluid communication between the interior volume of a compartment
and the exterior volume may be provided by a bundle of tube-shaped ducts.
[0016] In aspects, at least one duct may be at least one of curved and/or spiraled. In such
embodiments, the length of a duct may be significantly enlarged when compared to an
overall dimension of the duct, i.e. a linear distance between the inlet and the outlet
of a duct. The contact surface between the gases flowing through a duct and the walls
of the duct is consequently enlarged, increasing the heat exchange between the gases
and the walls. Also, a curved and/or spiraling flow path may per se yield a more intense
heat exchange with the walls compared to a straight flow path. Consequently, providing
a curved and/or spiraled duct supports reducing the temperature of the gas discharged
into the exterior volume. As a further effect, the increase of the overall flow path
length results in a delay of the discharge of the gases caused by the switching arc.
Accordingly, the hot gases with the unwanted reduction of dielectric withstand may
reach critical locations only well after the appearance of the peak transient recovery
voltage.
[0017] In non-limiting exemplary embodiments of the herein described circuit breaker with
metallic enclosure at least one duct is nozzle-shaped with the partial flow cross
section tapering from an upstream end to a downstream end in a direction from the
interior of the compartment to the exterior volume. In more particular embodiments
a downstream end of a first nozzle may be arranged to discharge into an upstream end
of a downstream duct, wherein further more in particular the upstream end of the downstream
duct may be in fluid communication with the exterior volume. The downstream duct may
be provided as a second nozzle, which in particular tapers form the upstream end to
a downstream end. These embodiments yield an ejector type arrangement, wherein the
high momentum fluid discharged from the first nozzle served to entrain fluid from
the exterior volume, which is mixed with the fluid discharged from the first nozzle
in the downstream duct. Thus, hot gas from inside the chamber flowing through the
first nozzle is effectively cooled through mixing with colder gas before being discharged
into the exterior volume. Two or more of the aforementioned ejector arrangements may
be arranged serially.
[0018] The ducts may in particular embodiments be manufactured by additive manufacturing
methods. This allows for more complex geometries and stronger convoluted ducts than
machining the ducts, while cost is significantly reduced when compared to assembling
the ducts from individual members.
[0019] In further aspects of the present disclosure, the chamber may comprise two axial
ends, wherein at least one axial end is provided with an end cap and further the ducts
are provided in the end cap. More in particular, the chamber may be axially divided
into the two compartments, such that each axial end of the chamber is an axial end
of one of the compartments. As such, it may be provided that each compartment comprises
a central end adjacent the other compartment and a free end which at the same time
constitutes an axial end of the chamber. Said free end may consequently, in embodiments,
be provided with the end cap as mentioned above. It is understood that the end cap
may be a separate member from the chamber and may be affixed to an axial end of the
chamber. The ducts may be provided by fixtures inside the end cap.
[0020] In further embodiments a circumferential wall of the end cap is provided with openings
so as to provide a fluid communication between the exterior volume and at least one
of the ducts.
[0021] The end caps, and in particular the fixtures inside the end cap which define the
ducts may be additively manufactured members, yielding essentially the benefits as
outlined above in connection with additively manufactured ducts.
[0022] In particular embodiments of the herein disclosed subject matter the tank is grounded,
that is electrically connected to the ground.
[0023] The dielectric gas contained inside the tank and the chamber may be carbon dioxide,
wherein the carbon dioxide further may or may not be combined with dioxide, i.e. molecular
O
2, and/or nitrogen, and/or an organofluorine compound selected from the group of a
fluoronitrile, a fluoroketone, a fluoroolefine, a fluoroether, an oxirane, a fluoroamine
and mixtures and/or by-products of said gases, and further including mixtures of said
organofluorine compound with carbon dioxide wherein the carbon dioxide further may
or may not be combined with dioxide, i.e. molecular O
2, and/or nitrogen.
[0024] Further disclosed is a method of manufacturing a circuit breaker with metallic enclosure
of the kind disclosed above. The method comprises providing a chamber. The chamber
is divided into two compartments electrically insulated from each other. A displaceable
switching actuator is provided inside at least one of the compartments. The switching
actuator is configured and adapted to selectively make electric contact between the
first and second compartments. The method comprises providing a tank enclosing the
chamber and providing a fluid communication between an interior volume of the chamber
and an exterior volume defined between a wall of the tank and the chamber. Further,
the tank is filled with a dielectric gas. Providing the fluid communication between
the interior volume of the chamber and the exterior volume defined between a wall
of the tank comprises providing a multitude of ducts. Providing the multitude of ducts
comprises manufacturing the multitude of ducts by an additive manufacturing method.
It is further understood that providing the ducts may comprise providing at least
one end cap comprising the ducts, wherein providing the end cap comprises manufacturing
the end cap by an additive manufacturing method. Providing the end cap may in particular
comprise attaching the end cap to an axial end of the chamber. More in particular,
an end cap may be attached to each axial end of the chamber.
[0025] In still further aspects a method of operating a circuit breaker with metallic enclosure
is disclosed. The circuit breaker comprises a chamber enclosing an interior volume
and comprising a first compartment and a second compartment. The first and second
compartments enclose the interior volume. The first and second compartments are electrically
insulated from each other. A switching actuator is provided inside at least one of
the compartments and configured and adapted to selectively provide electric connection
between the compartments. A sealed tank encloses the chamber and is electrically insulated
from the chamber, whereby an exterior volume is provided between a wall of the tank
and the chamber. Each of the compartments is connected to a line connector penetrating
the tank, wherein the penetration opening of each line connector through the tank
is sealed and the line connectors are electrically insulated from the tank. The tank
and the compartments contain a dielectric gas and the interior volume of each compartment
of the chamber is fluidly connected to the exterior volume. The method comprises one
of establishing and interrupting electric contact between the first and second compartments,
thereby inducing an arc, whereby the arc heats the gas inside the interior volume
and discharging the thus heated gas into the exterior volume.
[0026] In a first embodiment of said method the method comprises diffusing the stream of
heated gas discharged from the interior volume to the exterior volume prior to releasing
the heated gas into the exterior volume. Diffusing, in this respect, shall be understood
as splitting the entire stream of heated gas to be discharged up into a multitude
of partial streams which, upon entry into the exterior volume, get better dissipated
and admixed in the relatively cooler gas in the exterior volume, thus avoiding the
formation of plumes or strains of the heated gas in the exterior volume, that is,
between the compartments and the tank. The multitude of partial streams may count
at least 10, at least 15, at least 25 or at least 40. The multitude of partial streams
may count one of the aforementioned minimum values or more and 1000 or less.
[0027] In a second embodiment of said method the method comprises admixing the heated gas
which is discharged with gas from the exterior volume prior to releasing the heated
gas into the exterior volume. Thus, the temperature of the gas, upon being released
into the exterior volume, is significantly reduced when compared to the temperature
of the heated gas inside the interior volume.
[0028] In a third embodiment of said method the method comprises directing the heated gas
which is discharged through a multitude of ducts and cooling the heated gas which
is discharged while flowing through the multitude of ducts in exchanging heat with
the duct walls. In particular the length of each duct may be at least twice the hydraulic
diameter of the duct In more particular embodiments, the length of each duct may be
at least five times the hydraulic diameter of the duct. In even more specific exemplary
embodiments the length of each duct may be at least ten times the hydraulic diameter
of the duct. In certain embodiments the length of each duct may be one of the aforementioned
minimum values or more and 100 or less times the hydraulic diameter of the duct. The
multitude of ducts may count at least 10, at least 15, at least 25 or at least 40.
The multitude of ducts may count one of the aforementioned minimum values or more
and 1000 or less.
[0029] In a method of operating a circuit breaker with metallic enclosure as set forth above
the method steps of the above-described first through third embodiments may be combined
with each other. The circuit breaker may, while not limited to, be an embodiment of
a circuit breaker as herein described.
[0030] It is understood that the features and embodiments disclosed above may be combined
with each other. It will further be appreciated that further embodiments are conceivable
within the scope of the present disclosure and the claimed subject matter which are
obvious and apparent to the skilled person.
BRIEF DESCRIPTION OF THE DRAWINGS
[0031] The subject matter of the present disclosure is now to be explained in more detail
by means of selected exemplary embodiments shown in the accompanying drawings. The
figures show
- Fig. 1
- an exemplary embodiment of a circuit breaker with metallic enclosure;
- Fig. 2
- a first exemplary embodiment of providing fluid communication between the interior
volume of a compartment and the exterior volume enclosed between the chamber and the
wall of the tank;
- Fig. 3
- a second exemplary embodiment of providing fluid communication between the interior
volume of a compartment and the exterior volume enclosed between the chamber and the
wall of the tank;
- Fig. 4
- a further exemplary embodiment of providing fluid communication between the interior
volume of a compartment and the exterior volume enclosed between the chamber and the
wall of the tank; and
- Fig. 5
- still a further exemplary embodiment of providing fluid communication between the
interior volume of a compartment and the exterior volume enclosed between the chamber
and the wall of the tank;
[0032] It is understood that the drawings are highly schematic, and details not required
for appreciating the disclosed subject matter may have been omitted for the ease of
understanding and depiction. It is further understood that the drawings show only
selected, illustrative embodiments, and embodiments not shown may still be well within
the scope of the herein disclosed and/or claimed subject matter.
EXEMPLARY MODES OF CARRYING OUT THE TEACHING OF THE PRESENT DISCLOSURE
[0033] Figure 1 shows an exemplary embodiment of a circuit breaker with metallic enclosure
1 according to the present disclosure. Circuit breaker 1 comprises a tank 2 and a
chamber 3 enclosed by the tank. The tank commonly is grounded. Chamber 3 is supported
inside tank 2 by insulating supports 21 and surrounded by an exterior volume 211.
Chamber 3 comprises a first compartment 31 and a second compartment 32 which are disposed
along a common axis. Each compartment is connected to a line connector 312, 322. The
line connectors extent through the wall of the tank 2, whereas the openings through
which the line connectors extent are sealed so as to maintain a gas inside tank 2.
The line connectors are insulated from the tank. Each compartment 31, 32 encloses
an interior volume 311, 321, commonly forming an interior volume of the chamber. As
will be outlined below in more detail, the interior volume 311, 321 is fluidly connected
to the exterior volume 211. An insulator member 33 is provided axially between compartments
31 and 32 so as to electrically insulate compartments 31, 32 from each other. An axial
passageway is centrally provided through insulator member 33. Inside one of the compartments
a switching actuator 34 is provided. Switching actuator 34 is a rod which is axially
displaceable. Switching actuator 34 and the central passageway of insulator member
33 are adapted to each other so as to allow switching actuator 34 to advance through
the central passageway. Thus, switching actuator 34 is enabled to selectively close
and open and electric contact between the compartments. An actuation mechanism 35
is provided to effect displacement of switching actuator 34. End caps 4 are provided
on the axial ends of chamber 3. In each end cap 4 a multitude of ducts are provided
which establish fluid communication between the interior volume 311, 321 of the compartments
and the exterior volume 211. As noted, compartments 31, 32 are connected to line voltage,
while tank 2 is grounded. It is important that spark-over between the tank and the
compartments is avoided. To this extent the tank is filled with a dielectric gas,
and the distance between the walls of the tank and the compartments is chosen sufficiently
large that, in further consideration of the dielectric properties of the gas, spark-over
is avoided in minimum at a rated voltage. The gas contained within the interior volume
311, 321 of the compartments in addition has a further function. When the switching
actuator opens or closes the electric contact between the compartments, a switching
arc appears between switching actuator 34 and the second compartment 32. The gas is
intended to cool and quench the switching arc. Due to energy intake from the switching
arc the gas inside the compartments heats up and expands. In the gas is displaced
through the ducts in the end caps and into the exterior volume. Through the temperature
increase the dielectric withstand of the gas is reduced. Thus, in the presence of
heated gas spark-over may occur under conditions under which it would not in the presence
of gas of a lower temperature. Moreover, upon switching a transient increase of voltage
is observed, the so-called transient recovery voltage, which further increases the
risk of spark-over between the chamber and the tank, in particular if strains of heated
gas become present in the exterior volume 211 between the chamber and the wall of
the tank. This requires to provide a considerable margin against spark-over, which
means, for a given rated voltage and specific dielectric properties of the gas inside
the tank, that the distance between the chamber and the wall of the tank must be oversized.
Said problem may further be the more accentuated the lower the molecular weight and
heat capacity of the dielectric gas is. For instance, carbon dioxide yields a significantly
lower molecular weight and heat capacity than sulphur hexafluoride. That means, upon
a certain energy intake from the switching arc. temperature increase of the gas is
higher, and moreover the velocity at which the heated gas is discharged from the interior
volume 311, 321 into the exterior volume 211 is increased. This, on the one hand,
increases the likelihood of strains or plumes of heated gas being present in the exterior
volume, and further the likelihood of strains or plumes of heated gas being present
in the exterior volume at the time of the appearance of the peak transient recovery
voltage. Adding margin against spark-over in increasing the distance between the wall
of the tank and interior components being connected to line voltage increases the
space requirement of the circuit breaker, adds weight, and adds cost. Thus, according
to the present disclosure, the fluid communication between the interior volume 311,
321 and the exterior volume 211 is provided by a multitude of ducts having a length
which exceeds the hydraulic diameter. Thus, the discharge of heated gas from the interior
volume to the exterior volume may be delayed so that hot gas may reach critical locations
only well after the occurrence of the peak transient recovery voltage. Further, due
to providing an increased surface between the flow of heated gas and the material
of the duct walls, significant amounts of heat are transferred from the gas to the
solid material. Hence, the heated gas is significantly cooled down upon being discharged
through the ducts, and the degradation of dielectric withstand is significantly reduced.
In another aspect, it may be achieved that the heated gas, upon exiting the compartments,
is admixed with gas from the exterior volume, and the propensity of strains or plumes
of hot gas occurring is reduced. It may further be beneficial if the flow of gas discharged
into the exterior volume is directed away from the circumferential space between the
circumferential surface of the chamber, or the compartments, respectively, and the
wall of the tank. The propensity for spark-over to the tank is thus largely reduced
for a given combination of circuit breaker size, line voltage and dielectric gas.
For a given combination of rated voltage and dielectric gas, the size of the circuit
breaker can be reduced while maintaining the margin against spark-over to the tank.
This reduces space requirement, weight and cost.
[0034] Non-limiting exemplary embodiments of the ducts for discharging the heated gas from
inside the compartments to the exterior volume are disclosed in figures 2 - 5. Figure
2 shows a compartment 31 of a circuit breaker with an end cap 4. End cap 4 includes
a multitude of blades 41. The blades 41 subdivide the total flow cross-section provided
inside end cap 4 into a multitude of ducts between blades 41. The blades are shaped
so as to impose a swirling movement on the gases discharged from the interior 311
of compartment 31. The gases are discharged on a front face and a circumferential
surface of end cap 4. The axial velocity component of the gases exiting into the exterior
volume 211 is directed away from the compartment. The blades 41 provided in the end
cap provided a large heat exchange surface with the gas flowing through the ducts,
which serves to reduce the temperature of the heated gas being discharged from the
interior volume 311 to the exterior volume 211. Moreover, due to the non-linear, curved
flow path inside end cap 4 the delay time from the occurrence of the switching arc
until the heated gas actually enters the exterior volume 211 is comparatively large.
Accordingly, the actual discharge of the heated gas into the exterior volume may be
delayed until well after the time of occurrence of the peak transient recovery voltage.
In addition, the swirl imposed on the discharged heated gas may cause a mixing with
non-heated gas from the exterior volume and may thus serve to avoid or at least reduce
the occurrence of strains or plumes of heated gas in the exterior volume.
[0035] In a further embodiment shown in figure 3 the ducts inside the end cap 4 are provided
by chicane-shaped fixtures 42. The flow inside these ducts includes return flows which
intensify heat transfer from the gas to the fixtures. Moreover, low-pressure dead
wakes may serve to ingest non-heated gas from the exterior volume through openings
in the circumferential surface of the end cap, which intensely mixes with the heated
gas. The temperature of the heated gas may thus be largely reduced before being discharged
into the exterior volume 211. As with the embodiment of figure 2, the delay time from
the occurrence of the switching arc until the heated gas actually enters the exterior
volume 211 is comparatively large. Accordingly, the actual discharge of the heated
gas into the exterior volume may be delayed until well after the time of occurrence
of the peak transient recovery voltage. The gas discharged from the interior volume
311 is discharged into the exterior volume in a direction away from the chamber, or
the compartments, respectively.
[0036] According to an embodiment outlined in figure 4, the end cap comprises a multitude
of tube-shaped ducts 43 arranged in a bundle adjacent to each other. The tube-shaped
ducts may in particular embodiments exhibit honeycomb shaped cross sections. The tube-shaped
ducts have lateral openings which fluidly interconnect the ducts with each other and
with the exterior volume 211. The gas flowing through the ducts may thus ingest non-heated
gas from the exterior volume, thus reducing the temperature of the gas discharged
into the exterior volume at a downstream end of the ducts. Also in this embodiment,
the large surface/volume ratio of the ducts results in an intense heat exchange between
the gas and the walls of the ducts, which serves to reduce the temperature of the
gas flowing through the ducts. Depending on the length of the ducts the actual discharge
of the heated gas into the exterior volume may be delayed until well after the occurrence
of the peak transient recovery voltage. The gas discharged from the interior volume
is discharged into the exterior volume in a direction away from the chamber, or the
compartments, respectively.
[0037] In an exemplary embodiment shown in figure 5 the ducts through which the heated gas
is discharged from the interior volume 311 to the exterior volume 211 is provided
by nozzles 44 tapering from an upstream end to a downstream end in a direction from
the interior of the compartment to the exterior volume. The ducts comprise lateral
openings in that downstream of each nozzle an ingestion flow path is provided in fluid
communication with the exterior volume 211 on a circumferential surface of the end
cap 4. Hence, the fluid discharged from a nozzle 44 provides a motive force to ingest
non-heated gas from the exterior volume 211 into the ducts, thus mixing the heated
gas from the interior volume 311 with non-heated gas from exterior volume 211. The
nozzles thus work as ejectors. The temperature of the discharged gas is thus reduced.
As can be seen, nozzles are arranged to discharge into an upstream end of a downstream
duct, whereas the upstream end of the downstream duct is in fluid communication with
the exterior volume. In embodiments, a downstream duct may also be nozzle-shaped,
thus providing for a serial ejector arrangement. The temperature of the gas discharged
from the interior volume 311 is accordingly reduced by heat exchange with the walls
of the nozzles and further through ingestion of and mixing with non-heated gas from
the exterior volume 211. The overall length of the flow path provided may, as outlined
above, again result in a delayed discharge of gas from the interior volume into the
exterior volume, wherein the actual discharge of the heated gas into the exterior
volume may be delayed until well after the occurrence of the peak transient recovery
voltage. The gas discharged from the interior volume 311 is discharged into the exterior
volume in a direction away from the chamber, or the compartments, respectively.
[0038] While the subject matter of the disclosure has been explained by means of exemplary
embodiments, it is understood that these are in no way intended to limit the scope
of the claimed invention. It will be appreciated that the claims cover embodiments
not explicitly shown or disclosed herein, and embodiments deviating from those disclosed
in the exemplary modes of carrying out the teaching of the present disclosure will
still be covered by the claims.
1. A circuit breaker with metallic enclosure (1) comprising a chamber (3), the chamber
enclosing an interior volume (311, 312) and the chamber comprising a first compartment
(31) and a second compartment (32), wherein the first and second compartments enclose
the interior volume and wherein the first and second compartments are electrically
insulated from each other,
a switching actuator (34) displaceably provided inside at least one of the compartments
(31, 32) and configured and adapted to selectively provide electric connection between
the compartments, and
a sealed tank (2) enclosing the chamber and electrically insulated from the chamber,
whereby an exterior volume (211) is provided between a wall of the tank and the chamber,
wherein each of the compartments is connected to a line connector (312, 322) penetrating
the tank, wherein the penetration opening of each line connector through the tank
is sealed and the line connectors are electrically insulated from the tank,
wherein the tank and the compartments contain a dielectric gas and the interior volume
(311, 321) of each compartment of the chamber is fluidly connected to the exterior
volume (211) by a flow path having an overall flow cross section,
characterized in that the flow path between the interior volume of each of the compartments and the exterior
volume is subdivided into a multitude of ducts, each duct having a partial flow cross
section, a hydraulic diameter and a length, wherein the length of each duct is at
least twice the hydraulic diameter of the duct.
2. The circuit breaker with metallic enclosure (1) according to the preceding claim,
wherein at least one duct extends from an inlet adjacent the interior volume (311,
321) of a compartment (31, 32) to an outlet adjacent the exterior volume (211), and
wherein further a lateral fluid connection between the duct and the exterior volume
is provided and joins the duct between the inlet and the outlet.
3. The circuit breaker with metallic enclosure according to the preceding claim, wherein
at least one duct comprises a lateral opening in the duct wall.
4. The circuit breaker with metallic enclosure according to any preceding claim, wherein
the fluid communication between the interior volume (311, 321) of a compartment (31,
32) and the exterior volume (211) is provided by a bundle of tube-shaped ducts (43).
5. The circuit breaker with metallic enclosure according to any preceding claim, wherein
at least one duct is curved.
6. The circuit breaker with metallic enclosure according to any of the preceding claims,
wherein at least one duct is spiraled.
7. The circuit breaker with metallic enclosure according to any of the preceding claims,
wherein at least one duct (44) is nozzle-shaped with the partial flow cross section
tapering from an upstream end to a downstream end in a direction from the interior
(311, 321) of the compartment to the exterior volume (211).
8. The circuit breaker with metallic enclosure according to the preceding claim, wherein
a downstream end of a first nozzle is arranged to discharge into an upstream end of
a downstream duct, and further the upstream end of the downstream duct is in fluid
communication with the exterior volume (211).
9. The circuit breaker with metallic enclosure according to any of the preceding claims,
wherein the chamber (3) comprises two axial ends, wherein at least one axial end is
provided with an end cap (4), wherein the ducts are provided in the end cap.
10. The circuit breaker with metallic enclosure according to the preceding claim, wherein
the ducts are provided by fixtures (41, 42, 43, 44) inside the end cap (4).
11. The circuit breaker with metallic enclosure according to the preceding claim, wherein
a circumferential wall of the end cap (4) is provided with openings so as to provide
a fluid communication between the exterior volume and at least one of the ducts.
12. A method of manufacturing a circuit breaker with metallic enclosure according to any
of the preceding claims, comprising
providing a chamber (3) wherein the chamber is divided into two compartments (31,
32) electrically insulated from each other,
providing a displaceable switching actuator (34) inside at least one of the compartments
which is configured and adapted to selectively make electric contact between the compartments,
providing a tank (2) enclosing the chamber (3),
providing a fluid communication between an interior volume (311, 321) of the chamber
and an exterior volume (211) defined between a wall of the tank and the chamber, and
filling the tank (2) with a dielectric gas,
characterized in that providing the fluid communication between the interior volume (311, 321) of the chamber
and the exterior volume (211) defined between the chamber (3) and the wall of the
tank (2) comprises providing a multitude of ducts, wherein providing the multitude
of ducts comprises manufacturing the multitude of ducts by an additive manufacturing
method.
13. A method of operating a circuit breaker with metallic enclosure, the circuit breaker
comprising a chamber (3), the chamber enclosing an interior volume (311, 312) and
the chamber comprising a first compartment (31) and a second compartment (32), wherein
the first and second compartments enclose the interior volume and wherein the first
and second compartments are electrically insulated from each other,
a switching actuator (34) provided inside at least one of the compartments (31, 32)
and configured and adapted to selectively provide electric connection between the
compartments, and
a sealed tank (2) enclosing the chamber and electrically insulated from the chamber,
whereby an exterior volume (211) is provided between a wall of the tank and the chamber,
wherein each of the compartments is connected to a line connector (312, 322) penetrating
the tank, wherein the penetration opening of each line connector through the tank
is sealed and the line connectors are electrically insulated from the tank,
wherein the tank and the compartments contain a dielectric gas and the interior (311,
321) of each compartment of the chamber is fluidly connected to the exterior volume
(211),
the method comprising one of establishing and interrupting electric contact between
the first and second compartments, thereby inducing an arc,
whereby the arc heats the gas inside the interior volume, and discharging the thus
heated gas into the exterior volume, characterized in that discharging the heated gas into the exterior volume comprises diffusing the heated
gas which is discharged from the interior volume to the exterior volume prior to releasing
it into the exterior volume.
14. The method of the preceding claim, characterized in admixing the heated gas which is discharged with gas from the exterior volume prior
to releasing the heated gas into the exterior volume.
15. The method of any of the two preceding claims characterized in directing the heated gas which is discharged through a multitude of ducts, and cooling
the heated gas which is discharged while flowing through the multitude of ducts in
exchanging heat with the duct walls, wherein in particular the length of each duct
is at least twice the hydraulic diameter of the duct.