[0001] The invention relates to a method for cooling an object, in particular a metal wire
or a metal tube, wherein a jet of a cold gas is blown onto said object. Further the
invention is related to a device for cooling an object comprising a passage way for
said object and a gas blowing device with gas outlets for directing a cold gas to
said passage way.
[0002] Pending German Patent Application Number
DE 10 2004 054 627 (not yet published) discloses a device for cooling long objects, for example tubes,
by blowing cold gas onto the object. The device comprises a first chamber with a plurality
of nozzles for blowing out cold gas jets. Further, an enveloping tube is provided
which envelopes the object. The cold gas blown out of the first chamber flows between
the object and the enveloping tube and thereby additionally cools down the object.
[0003] The device disclosed in the above-mentioned German Patent Application shows a good
heat contact between the cold gas and the object. However, to enhance the heat transfer
coefficient the warmed gas should be removed as fast as possible from the object to
be cooled. Otherwise it will form an insulating gas buffer.
[0004] Therefore, it is an object of the present invention, to provide an improved method
and an improved device for cooling an object by blowing gas jets onto it.
[0005] This object is achieved by method for cooling an object, in particular a metal wire
or a metal tube, wherein a jet of a cold gas is blown onto said object, which is characterized
in that said object is cooled in indirect heat exchange with a liquefied gas, said
liquefied gas is then evaporated to produce said cold gas and said cold gas is blown
onto said object.
[0006] The inventive device for cooling an object comprises a passage way for said object
and a gas blowing device with gas outlets for directing a cold gas to said passage
way wherein a heat exchange passage for a liquefied gas and means for evaporating
said liquefied gas in order to produce a cold gas are provided, wherein said heat
exchange passage for said liquified gas is in heat exchange contact with said passage
way for said object.
[0007] According to the invention the cold of a liquefied gas is utilized to cool the object
in two steps:
[0008] First, the liquefied gas is brought into indirect heat exchange with the object.
The liquefied gas flows through heat exchange passages which are arranged close to
the passageway where the object is placed into or passed through. By convection of
the atmosphere surrounding the object heat is transferred to the liquefied gas. In
addition, especially when cooling hot objects with a temperature above 500 °C there
is a substantial temperature difference between the hot object and the liquefied gas.
Thus, part of the heat is transferred to the liquefied gas by radiation.
[0009] Then the liquefied gas is evaporated to produce a cold gas. Part of the liquefied
gas might already have been evaporated during the indirect heat exchange of a liquefied
gas with the object.
[0010] Finally, the cold gas is blown onto the object to directly exchange heat with the
object. By the inventive method the cold of a liquefied gas is highly efficiently
utilized.
[0011] Preferably, liquid nitrogen is used as liquefied gas.
[0012] According to a preferred embodiment of the invention said heat exchange passages
for the liquified gas are arranged around said gas blowing device. By that arrangement
the indirect cooling by the liquified gas and the direct cooling by means of jets
of cold gas is carried out at the same place. The space for cooling the object, for
example the metal tube, is thus minimized.
[0013] The liquified gas is passed through heat exchange passages to indirectly cool the
object. Preferably these heat exchange passages are designed as a spiral winded around
the passageway where the object to be cooled is passed through. More preferably the
spiral pipeline for the liquified gas is winded around the gas blowing device.
[0014] After having indirectly cooled the object the liquified gas is transferred to an
evaporator where the liquified gas is evaporated, for example in indirect heat exchange
with air or water. The resulting cold gas is fed to the gas blowing device, blown
out through gas outlets and directed to the object. Preferably the gas blowing device
also comprises gas inlets arranged close to the passageway for the object. Gas which
has been warmed up in heat exchange with the hot object can be withdrawn very quickly
by means of these gas inlets. Thus, the heat transfer coefficient is essentially improved.
It is preferred to utilize a fan or a similar device to suck in warm gas from the
passageway into the gas inlets.
[0015] The invention is preferably suitable for cooling metal objects, such as tubes, wires
or sheets, after a heat treatment. The inventive device can be placed in-line with
the heat treatment process.
[0016] The invention as well as further details of the invention shall now be described
with reference to the accompanying drawings.
Figure 1 shows an inventive device for cooling hot metal tubes.
Figure 2 shows an alternative arrangement of the inventive gas cooling device.
Figure 3 shows another embodiment of the gas blowing device.
[0017] Figure 1 illustrates the principle of the invention. The inventive method is preferably
be used for cooling hot metal tubes 1 after a heat treatment process when they have
a temperature of approximately 1000 °C.
[0018] From a storage tank 2 liquid nitrogen is transferred to a spiral pipeline 3. In the
center of the spiral pipeline 3 there is a passage way where the hot tube 1 is transported
through. Tube 1 is thus in indirect heat exchange with the liquid nitrogen.
[0019] There are two heat transfer mechanisms active: First, heat is transferred from the
tube 1 to the spiral pipeline 3 by convection of the surrounding atmosphere. Second,
due to the large temperature difference the spiral pipeline 3 and tube 1 there is
a significant heat transfer by radiation.
[0020] After leaving spiral pipeline 3 the nitrogen partly evaporated, partly still in liquid
phase, flows to an evaporator 4. In evaporator 4 the nitrogen is completely transferred
into the gaseous phase. The resulting nitrogen gas is fed to a gas blowing device
5 via pipeline 6. There, the gas is distributed to several gas outlets 7 which are
arranged around the passage way for tube 1. The nitrogen gas is blown out of the gas
outlets 7 and directed to tube 1.
[0021] Gas outlets 7 are alternately disposed with gas inlets 8. The nitrogen which has
been warmed up by tube 1 is sucked into the gas inlets 8 and withdrawn through line
9.
[0022] Figure 2 shows another arrangement of the gas blowing device 5 and the spiral pipeline
3. The gas blowing device 5 as well as the spiral pipeline 3 are in principle of the
same design as shown in figure 1. However, the gas blowing device 5 is disposed within
in the center part of the spiral pipeline 3.
[0023] The advantage of the arrangement according to figure 2 is that cooling is achieved
within a shorter length and that the nitrogen gas blown out of gas outlets 7 is also
cooled by the liquid nitrogen flowing in spiral pipeline 3. Further, the forced flow
of the nitrogen gas out of gas outlets 7 and into gas inlets 8 also enhances the convective
heat transfer to spiral pipeline 3. On the other hand, the radiative heat transfer
is reduced since part of the spiral pipeline 3 is in the shape of the gas blowing
device 5.
[0024] Figure 3 illustrates another embodiment of the inventive gas blowing device especially
designed for cooling of wires. For sake of simplicity, the spiral pipeline 3 is not
shown in this figure. The spiral pipeline 3 may be arranged as shown in figure 1 or
in figure 2. Gas feed pipeline 6 for feeding the evaporated nitrogen gas to the gas
outlets 12, 14 and pipeline 9 for withdrawing the warm nitrogen gas are also not shown
in figure 3.
[0025] The gas blowing device comprises two wind boxes 10, 11 positioned opposite to each
other on both sides of the passage way for wire 1. Both wind boxes 10, 11 comprise
gas outlets 12, 14 and gas inlets 13, 15. The gas outlets 12 and the gas inlets 13
of wind box 10 are arranged alternately. The same applies for wind box 11. In addition,
gas outlets 12 and gas outlets 14 of wind boxes 10 and 11 are positioned crosswise.
That means, opposite gas outlet 12 of wind box 10 there is gas inlet 15 of wind box
11. Thus, the cold gas is blown out of gas outlet 12, flows around wire 1 is sucked
into gas inlet 15. And gas which is directed to wire 1 via a gas outlet 14 of wind
box 11 is withdrawn through that gas inlet 13 of wind box 10 which is positioned directly
opposite to gas outlet 14.
1. Method for cooling an object (1), in particular a metal wire or a metal tube, wherein
a jet of a cold gas is blown onto said object (1), characterized in that said object (1) is cooled in indirect heat exchange (3) with a liquefied gas (2),
said liquefied gas is then evaporated (4) to produce said cold gas and said cold gas
is blown (5) onto said object (1).
2. Method according to claim 1 characterized in that liquid nitrogen is used as liquefied gas (2).
3. Device for cooling an object (1) comprising a passage way for said object (1) and
a gas blowing device (5) with gas outlets (7) for directing a cold gas to said passage
way, characterized in that a heat exchange passage (3) for a liquefied gas and means (4) for evaporating said
liquefied gas in order to produce a cold gas are provided, wherein said heat exchange
passage (3) for said liquified gas is in heat exchange contact with said passage way
for said object (1).
4. Device according to claim 3 characterized in that said heat exchange passage (3) for said liquified gas is arranged around said gas
blowing device (5).
5. Device according to any of claims 3 or 4 characterized in that said heat exchange passage (3) for said liquified gas is designed as a spiral winded
around said gas blowing device (5).
6. Device according to any of claims 3 to 4 characterized in that said gas blowing device (5) comprises gas inlets (8) directed to said passage way.
7. Device according to claim 6 characterized in that said gas inlets (8) and said gas outlets (7) are disposed on two opposite sides of
said passage way and that each of said gas inlets (8) is positioned opposite one of
said gas outlets (7).