U.S. patent number 3,642,061 [Application Number 04/813,438] was granted by the patent office on 1972-02-15 for heat exchanger.
This patent grant is currently assigned to Stein & Roubaix. Invention is credited to Raymond Waeselynck.
United States Patent |
3,642,061 |
Waeselynck |
February 15, 1972 |
HEAT EXCHANGER
Abstract
A heat exchanger from which is absent a dividing wall between an
axial flow of hot fluid, preferably a flame, and an encircling
spiral flow of fluid to be heated which is maintained separate by
the centrifugal force due to its cyclonic flow and is contained by
a refractory-lined wall which absorbs radiant heat from the hot
fluid.
Inventors: |
Waeselynck; Raymond (Paris,
FR) |
Assignee: |
Stein & Roubaix (Paris,
FR)
|
Family
ID: |
8649012 |
Appl.
No.: |
04/813,438 |
Filed: |
April 4, 1969 |
Foreign Application Priority Data
Current U.S.
Class: |
165/111;
60/39.183; 126/110C; 432/29; 432/223; 60/39.55; 165/169; 432/219;
165/DIG.162 |
Current CPC
Class: |
F02G
1/057 (20130101); F22G 1/00 (20130101); F22D
1/26 (20130101); F23R 3/005 (20130101); F02C
6/06 (20130101); F02G 2258/10 (20130101); Y10S
165/162 (20130101) |
Current International
Class: |
F22G
1/00 (20060101); F22D 1/00 (20060101); F23R
3/00 (20060101); F02G 1/00 (20060101); F02C
6/00 (20060101); F02C 6/06 (20060101); F02G
1/057 (20060101); F22D 1/26 (20060101); F28c
003/00 () |
Field of
Search: |
;165/1,111,156,169
;60/39.66,39.18C ;263/19A ;126/11C |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Davis, Jr.; Albert W.
Claims
I claim:
1. A heat exchanger comprising an outer hollow casing, and an inner
hollow casing supported internally of said outer casing and
annularly spaced from the latter, said outer casing including an
inlet conduit axially extending into said inner casing and
annularly spaced therefrom, said inlet conduit being adapted for
supplying a preheated gas into said inner casing, said inner casing
including a preheated gas outlet coaxially opposite said inlet
conduit for expelling said preheated gas, said inner casing being
axially spaced from said inlet conduit, the annular space between
said inner and outer casings constituting an inlet passageway for
supplying a gas to be heated into said inner casing through the
axial space between said inlet conduit and said inner casing, said
inner casing including an inner wall and helical vanes helically
extending along said inner wall between said inlet conduit and said
preheated gas outlet, said helical vanes being directly exposed to
said preheated gas and adapted for passing said gas to be heated
helically through said inner casing in exposing relation to said
preheated gas, said inner casing including inlet vanes for
directing said fluid to be heated tangentially thereinto to engage
said helical vanes, said inner casing including a further outlet
for expelling said gas to be heated, said further outlet including
a portion annularly surrounding said preheated gas outlet and
disposed adjacent said inner wall of said inner casing.
2. Apparatus as claimed in claim 1 wherein the wall of the inner
casing has a lining of refractory material absorbing radiation from
said hot fluid.
3. Apparatus as claimed in claim 1 including means for maintaining
said inner casing under pressure.
4. Apparatus as claimed in claim 1 including a conventional heat
exchanger connected to receive heated fluid from said further
outlet.
Description
The present invention concerns an apparatus in which two fluids
flow and exchange heat.
In heat exchangers of known type, the two fluids flow on either
side of a fluidtight wall, which is at the same time the seat of
the heat exchange, this wall being that of tubes, flues, etc. The
wall has to resist thermal and mechanical stresses as well as
chemical attacks resulting from the elevated temperatures to which
it is subjected. Its price is therefore high, its reliability is
problematical and the exchange temperatures are limited to values
compatible with its resistance. Finally, if one or the other of the
wall faces is exposed to a corrosive fluid or a fluid charged with
impurities, the deposits formed are dangerous for the safety of the
heat exchanger and reduces to its efficiency.
The present invention relates to a heat exchanger which does not
have the above-mentioned disadvantages because of the absence of
separation walls between the two heat-exchanging fluids.
An apparatus according to the invention comprises an enclosure of
revolution, equipped with an axial admission and discharge for the
passage of the hot fluid, a tangential admission and discharge for
the fluid to be heated and means for ensuring rotation of the fluid
to be heated at a velocity sufficient for the centrifugal force to
maintain it in the vicinity of the wall of the enclosure between
the tangential admission and discharge.
The internal wall of the enclosure is preferably lined with a
refractory material insensitive to attack at the high temperature
of the fluid to be heated with which it is in contact, having an
absorbent power as close as possible to that of black body
absorption, and having a surface as extended as possible, arranged
for promoting convection but for limiting turbulence in contact
with the fluid to be heated. For example, the refractory material
lining, which may be of steel, ceramic, etc., may comprise sections
of helical fins.
The hot fluid passing axially through the enclosure may result from
combustion controlled to produce a flame of large surface which
radiates strongly.
In one embodiment of the exchanger according to the invention one
or more longitudinal slits are provided in the wall of the
enclosure for recovering the solid particles which may be taken up
by the fluid to be heated, the apparatus then acting simultaneously
as a separating cyclone.
In an exchanger according to the invention, the axial hot fluid
heats by radiation the internal surface of the enclosure, which
restores this heat by convection to the fluid to be heated having a
helical movement. The hot fluid may result, for example, from the
combustion of oil fuel, while the fluid to be heated may be air,
for example. The differences in the angular velocities, densities
and viscosities are practically opposed, as shown by experience, to
mixing of the combustion gases and air to be heated, such that the
latter is practically uncontaminated if its removal at the outlet
is suitably limited by a closure device. The combustion gases which
leave at a temperature which is still high, may be sent to a boiler
or a conventional heat exchanger, in which the fuel and combustion
air are preheated before their introduction into the burner with
which the apparatus according to the invention is equipped.
This type of heater according to the invention, in which exchanges
at the highest temperatures occur without an intermediate wall,
does not have most of the disadvantages of conventional exchangers.
Thus, the convection surfaces, which may be cut out as desired, are
practically not subjected to either thermal or mechanical stresses;
their expansion takes place freely and fluidtightness is not
necessary; they are protected from contact with the combustion
gases and are consequently insensitive to their attack; they have
simply to resist the chemical attack of the fluid to be heated
which, in most cases, is a clean and homogeneous, possibly neutral,
gas. Finally if deposits are produced, their effect is not to
destroy but to protect the walls against radiation; at the most
they may modify their coefficient of absorption.
The efficiency of the exchanger according to the invention, defined
as the ratio of the quantity of heat exchanged by radiation to the
calorific value of the fuel, is higher, the higher is the
temperature of the flame itself, that is to say, the higher the
temperature to which the combustion air has been previously heated.
When the fluid to be heated is not air, the burner receives its
combustion air separately. In the case where the fluid to be heated
is air, if the heat exchanged by radiation represents for example
50 percent of the calorific value of the fuel, and if the
combustion air is admitted at a temperature of 400.degree. C., it
is sufficient to take a small fraction (about one-fourth) of the
total air to ensure combustion, the principal part of the air being
heated to 800.degree. or 900.degree. C. by contact with the
wall.
This type of heater will find applications whenever it is a matter
of heating a fluid in which a slight entrainment of combustion gas
is not a serious disadvantage. It may be applied for example to the
feeding of two gas turbines operating simultaneously: in one of
them the combustion gases are expanded after their passage through
a conventional exchanger (boiler, tubular air heater), which
reduces their temperature to a value acceptable for the gas turbine
(for example 630.degree. C. if the fuel is unrefined heavy fuel);
the other gas turbine receives the gases which are uncontaminated
and are heated to high temperature (for example 800.degree. to
900.degree. C.), and the weight of which is several times that of
the combustion gases. Despite the use of unrefined heavy fuel, the
second gas turbine, which is much larger, thus operates on a
thermodynamic cycle of high efficiency without danger of
corrosion.
The following additional description, with reference to the
accompanying drawings, given mainly as an example, is intended to
illustrate the invention.
In these drawings:
FIG. 1 is a diagrammatic axial section of a radiation gas heater
according to the invention;
FIG. 2 shows diagrammatically an exchanger according to the
invention used for the feeding of gas turbines, and
FIG. 3 is a diagram showing the application of the invention to
heating the superheaters of a boiler.
A fluid heater according to the invention, such as is shown in FIG.
1, comprises an enclosure of revolution 1, for example cylindrical,
conical etc., provided with an axially arranged inlet 2 and outlet
3. The inlet 2 may receive a hot combustion-supporting gas
associated with a fuel inlet conduit 4, or a combustible mixture,
intended to burn in the interior of the enclosure, the outlet 3
serving for the outflow of the hot gas formed of the combustion
gases in the example shown. The enclosure also comprises an inlet 5
and a tangential outlet 5a for the fluid to be heated. For this
purpose, a volute, vanes, etc., may be provided. The cold fluid set
in rotation, for example by the vanes 7, ought to have a sufficient
velocity for it to be kept by the centrifugal force in the vicinity
of the wall 1 along the entire length of the latter. The inlet for
the fluid to be heated is generally so arranged that this fluid and
the heating fluid are in parallel currents; it may, however, also
be such that the flows are in countercurrent. The first possibility
is used in the embodiment of FIG. 1, where the tangential inlet 5
is close to the inlet 2, while the tangential outlet 5a is close to
the axial outlet 3. The intake of the heated fluid is regulated by
varying the relative vacuum in the outlet conduit 6.
In addition, the wall of the enclosure 1 is preferably provided
with helical convection vanes 8.
Finally, in the embodiment shown, there is provided some preheating
of the air, which entering at 9 flows along the enclosure 1, owing
to a jacket 10 concentric with this wall, before being admitted at
5 through the vanes 7.
Such an apparatus is of simple construction and does not
necessitate the provision of material resistant to very high
temperatures, the wall of the enclosure 1 being continuously cooled
by the fluid to be heated. The risk of corrosion of the walls is
thus obviated.
The exchanger may be used for heating any gaseous or liquid fluid.
In the latter case, it may be used, for example, for the
gasification of any liquid (including a fuel), the latter being
preferably finely sprayed in the gas already produced and carried
in closed circuit in contact with the wall of the exchanger.
If the fluid to be heated is air, the latter may be used for
domestic purposes; indeed, the apparatus may be regulated such that
the air is practically free from combustion gases.
FIG. 2 shows the application of an exchanger according to the
invention to the feeding of a mixed installation generating power
from two gas turbines. In this case, the furnace is at the pressure
prevailing upstream of the turbines; the turbine 11, by far the
more powerful, has passing through it the clean gas 14, heated to
an elevated temperature, for example 850.degree. C.; the turbine 12
receives only the combustion gases after the latter have been
cooled in an exchanger 15 to a temperature compatible with the use
of gases containing flue dust and corrosive gases, for example
630.degree. C. As indicated in the foregoing, the exchanger 15 may
serve either to heat the clean gas (for example air) and combustion
air before their introduction 16 into the furnace 13, or to produce
or superheat steam, or to heat boiler feed-water. Finally, the
clean gas may flow in a closed circuit and under high pressure,
passing successively through the furnace 13, turbine 11 and
cooler-exchangers before being reintroduced into the inlet of the
compressors. The combustion gases, on the contrary, are discharged
to the outside after passing through the turbine 12 and the outlet
exchangers or economizers. However, these combustion gases may be
neutralized, purified and filtered wholly or in part, so as to form
the gas of the actual circuit, and compensate any losses of the
latter.
Another application of the invention is that of heating boiler
superheaters (or any other high-temperature exchangers) according
to the diagram of FIG. 3.
The heater furnace according to the invention and here shown at 18,
produces a high-temperature neutral gas 19, which passes through
the conventional tubular exchanger 20 (superheater, resuperheater,
complete boiler, or any heater), and flows in a closed circuit
owing to a pickup blower 21 which makes good the pressure losses.
The furnace 18 acts as a cyclone and eliminates any solid particles
in suspension. These particles are discharged from time to time
from the furnace, the internal wall of which comprises at least one
longitudinal slit acting as a dust trap, and some orifices, through
which this dust is intermittently driven. The gas in circulation is
clean, and the attacks by erosion or corrosion at elevated
temperature are reduced.
By varying the speed of the blower 21, the level of the exchanges
in 20 may be regulated; for example, the superheat temperature may
be regulated if 20 is a superheater.
This application is particularly interesting in the case of an
installation with a mixed gas-steam cycle, with a boiler through
which the gases pass under pressure, where the furnace 18 is under
pressure and 20 is the high-temperature part of the boiler, while
the evaporator tube nest is situated at the outlet of the
combustion gases from the furnace 18. The use of a clean gas in 20
eliminates the serious risks of rapid fouling and permits the use
of compact tube nests. In addition, the limitation to 800.degree.
or 850.degree. C. of the temperature of the gas passing through 20
considerably reduces the risk of bursting or rupturing of the tubes
by overheating in case of difficulty in the circulation or abrupt
variation in load. The gas turbine is then fed by an offtake at 22
of clean and hot gas upstream of the exchanger 20, the replacement
gas arriving at 23 upstream of 21.
Another application is that of heating without oxidation before
forging, rolling or wire-drawing, or the heat treatment in
controlled atmosphere of various metallurgical products (tubes or
parts of high-alloy steel, or of nonferrous metals, for example).
In this case, it is merely necessary to suitably select the gas
passing through the container 20 in which the parts to be heated
are placed.
An exchanger constructed in accordance with the invention may also
be used in drying installations. It is in fact known that drying
installations necessitate the production of a considerable flow of
fluid at elevated temperature, and also a mechanical device for
conveying the materials to be dried. These two conditions may be
met by an exchanger according to the invention; for this purpose,
the exchanger is selected to have a sufficient working pressure for
the combustion gases to feed a turbine serving for the mechanical
conveying of the materials to be dried; the hot fluid, consisting
of air, is thus at a high pressure and is therefore expelled from
the apparatus at a high velocity. The range of regulation of the
apparatus will be so much greater if in this case it is possible to
accept a certain proportion of combustion gases in the hot air.
Yet another application is that of heating living rooms, the clean
gas being then simply air which, heated directly in the furnace,
leaves the latter almost free from any trace of combustion
gases.
It is obvious that the embodiments described have been given mainly
as examples and that they may be given numerous modifications
without going beyond the scope of the present invention. The
application examples are also not restrictive, the apparatus
according to the invention being utilizable in all cases where a
very simple heater is desired and where very slight pollution by
combustion products is not embarrassing.
* * * * *