U.S. patent number 3,850,417 [Application Number 05/316,694] was granted by the patent office on 1974-11-26 for system for accelerated cooling of loads in controlled atmosphere forced circulation type furnaces.
This patent grant is currently assigned to Guinea Hermanos Ingenieros, S.A.. Invention is credited to Salvador Guinea Elorza.
United States Patent |
3,850,417 |
Elorza |
November 26, 1974 |
SYSTEM FOR ACCELERATED COOLING OF LOADS IN CONTROLLED ATMOSPHERE
FORCED CIRCULATION TYPE FURNACES
Abstract
A system for the accelerated cooling of loads in controlled
atmosphere forced circulation type furnaces having a central
ventilator includes a gas cooling chamber at the base of the
furnace equipped with a water cooled coil. The chamber is between
the refractory insulator and the metal plate which constitutes the
base platform in such a way that gas can enter the chamber through
collection valves. An annular space for the return of cooled gas is
provided between the chamber and the protective bell.
Inventors: |
Elorza; Salvador Guinea
(Bilbao, ES) |
Assignee: |
Guinea Hermanos Ingenieros,
S.A. (Bilbao, ES)
|
Family
ID: |
23230230 |
Appl.
No.: |
05/316,694 |
Filed: |
December 20, 1972 |
Current U.S.
Class: |
266/254; 165/103;
266/256; 266/259 |
Current CPC
Class: |
C21D
9/663 (20130101) |
Current International
Class: |
C21D
9/663 (20060101); C21D 9/54 (20060101); C21d
009/46 () |
Field of
Search: |
;266/5R,5B,5C
;165/61,103,104 ;432/77,256 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
455,089 |
|
Oct 1936 |
|
GB |
|
1,046,082 |
|
Dec 1958 |
|
DT |
|
Primary Examiner: Lake; Roy
Assistant Examiner: Bell; Paul A.
Attorney, Agent or Firm: Wenderoth, Lind & Ponack
Claims
I claim:
1. A system for accelerating the cooling of a load in a furnace
having a centrally located ventilator fan for recirculating gas
through a main furnace chamber containing said load, said system
comprising:
an insulating-refractory layer positioned beneath said main furnace
chamber, said fan being positioned on top of said
insulating-refractory layer centrally thereof in said main furnace
chamber, whereby gas recirculated by said fan is directed radially
outwardly from said fan above said insulating-refractory layer;
a bottom metal plate forming the base of said furnace spaced below
said insulating-refractory layer;
said insulating-refractory layer and said plate forming
therebetween a cooling chamber;
cooling coils positioned within said cooling chamber;
an annular space continuously connecting the outermost extent of
said cooling chamber with said main furnace chamber;
a plurality of openings extending upwardly through said
insulating-refractory layer from said cooling chamber, at positions
inwardly of said outermost extent thereof, to said main furnace
chamber at positions thereof immediately adjacent the periphery of
said fan;
collecting valve means vertically movable in each of said openings,
from a first lower position not interferring with said gas directed
radially outwardly from said fan, to a second upper position
interferring with said gas directed radially outwardly from said
fan; and
each of said collecting valve means having thereon means directed
toward said periphery of said fan for intercepting substantially
all of said gas directed radially outwardly from said fan, when
said collecting valve means are in said second position, and for
directing said thus intercepted gas through said openings into said
cooling chamber, whereafter said gas is cooled in said cooling
chamber, passed through said annular space into said main furnace
chamber thereby cooling said load, and then returned to said
fan.
2. A system as claimed in claim 1, wherein said means for
intercepting on each of said collecting valve means comprises a
cut-out portion forming a curved concave gas collecting
surface.
3. A system as claimed in claim 1, further comprising a gas
diffuser positioned in said main furnace chamber on top of said
insulating-refractory layer and peripherally surrounding said fan;
said diffuser having an outer guide plate means for directing said
gas directed radially outwardly from said fan upwardly into the
outer extent of said main furnace chamber, when said collecting
valve means are in said first position; said diffuser having
substantially radially inwardly extending vanes for directing said
gas outwardly from said periphery of said fan to said outer guide
plate means.
4. A system as claimed in claim 3, wherein alternate of said vanes
extend inwardly to positions immediately adjacent said periphery of
said fan, the remainder of said vanes extending inwardly to
positions spaced from said periphery of said fan, said openings
being located between the innermost ends of said remainder of said
vanes and said periphery of said fan.
5. A system as claimed in claim 1, further comprising additional
cooling coils rigidly attached to said bottom metal plate
exteriorly of said cooling chamber.
6. A system as claimed in claim 1, wherein said collecting valve
means are vertically movable to positions intermediate said first
and second positions.
Description
BACKGROUND OF THE INVENTION
The cooling system of the invention relates principally to cold
rolled steel plate annealing furnaces. The importance of such
systems is great since they are basic to the manufacture of
automobile bodies, tinplate and other products, and since they
continuously replace other systems customarily utilized in the
manufacture of steel plate. Consequently, this occasions a growing
number of installations complementing the major iron and steel
plants. This type system can also be applied, naturally in bell
furnaces at all times, for annealing other ferrous and non-ferrous
materials and, on occasion, in other types of furnaces.
In order to better understand the application of this new cooling
system and to more clearly grasp the advantages it offers in
relation to those currently employed, we will briefly recall the
features of a bell furnace, its operation, and summary of the more
frequently used cooling processes.
Bell furnaces are units of varying size which can take loads from
some hundred kilograms up to 50 tons and more. As stated, many of
these are used for annealing cold rolled steel plate.
Each unit is constituted by: the so-called heating bell, because of
its shape, which is a movable component containing the electrical
resistors, radiating or burning tubes, heat generators, and thermal
insulation, lining, metal frame, etc.
Each unit also includes one or more bases on which the load is
placed, and which when operational are covered by means of a
so-called protective bell insulating the load from outside air. Air
is replaced inside the protective bell by a protective environment
the purpose of which is to prevent oxidizing of the load during the
process.
In order to have uniform temperature at all points of the loads and
to accelerate the heating and cooling processes, there is a
ventilator fan or propeller which causes gas circulation,
interchanging the heat with the protective bell, transmitting it to
the load during the heating period or, inversely, transmitting that
of the load to the outside during the cooling stage. To this
interchange there is added, of course, that heat generated by
radiation.
The number of bases required to obtain maximum performance of each
unit depends on the cycle to be followed, heating and cooling time,
loading and unloading, container cleansing, etc., since the heating
bell must be continuously heating certain of the bases while the
others go through the indicated stages successively.
As is deduced, cooling time is of importance for utilization of the
bases, for which reason the major specialized enterprises in the
world devote much effort to the development and study of procedures
for accelerating such cooling. Rapid cooling enables the reduction
of the number of bases for the same production, with consequent
advantages with respect to size of plants, reduced costs, etc.
Also of interest is the possibility of modernizing existing plants,
increasing production merely by adding heating bells while
maintaining the number of bases.
In sum, performance of a unit is as follows: The load to be
treated, generally several coils, is deposited on a base. The load
is then covered by means of a protective bell limiting the space to
be occupied by the controlled atmosphere, the corresponding
cleansing is effected, and the complete system is covered with the
heating bell. This latter is energized and the base temperature, as
well as that of the protective bell and load, commences to rise
until it reaches that necessary for the treatment. This temperature
is maintained for sufficient time or, if a special treatment is
involved, it can be varied according to an established plan.
The necessary thermal energy to effectively carry out the desired
treatment having been furnished, the heating bell is removed and
the cooling process is initiated in the protective bell. When
cooling terminates, the base is unloaded following removal of the
protective bell. A first base is now ready to restart the
cycle.
Meanwhile, a second base will be in one of the earlier stages of
heating, cooling, etc., and in order that the heating bell may
always be functional, a number of bases will be necessary. This
number will be dependent on the duration of the successive
operations, and may be two, three, four, five or more in special
cases.
Cooling of bell furnaces in conventional installations is effected
by interchanging heat between the load and the exterior. This is
effected by conductivity through the plate of which the protective
bell is formed.
Load heat passes to the bell by radiation and convection and, thus
to the outside. As stated, cooling is accelerated as a result of
forced circulation maintained inside the protective bell. In order
to achieve the same effect, it is possible to accelerate outside
air circulation to the bell by means of the corresponding
installations and at times the exterior of the bell is even sprayed
with cold water.
As previously noted, world specialists seeking increasingly rapid
cooling to improve the efficiency of the furnaces indicated,
studied and patented several procedures which have been used with
varying degrees of success.
Certain of these prior cooling procedures will now be
considered.
One procedure consists in extracting through the base a part of the
gas circulating inside the furnace by means of a pipe, cooling it
in a coil submerged in water and subsequently returning it to the
regular system. Naturally, this entire cycle is impelled by the
base ventilator fan and normally there should be two coolers per
base.
Another system consists in a similar operation. However, gas
movement and its passage through the auxiliary cooling system is
effected by means of an independent ventilator fan.
Finally, a rather well known third procedure consists in placing a
given number of refractory steel coils in the gas current proper
arranged in the base and on the most appropriate points of the gas
distribution diffuser. Water is conveyed through these coils during
the cooling phase.
All of the procedures described suffer from some drawback not
presently resolved and which include the following:
The first procedure collects only a part of the circulating gas
which part can be estimated to be one fourth to one eighth of the
entirety. This requires voluminous installations under the base
which in turn requires special fondations, it being necessary to
have a true basement rather than a simple foundation.
From the foregoing it is clear that this procedure is costly to
install and can well be prohibitive when it is proposed to
modernize plants where such a circumstance has not been
foreseen.
Under the second procedure a greater amount of circulating gas can
be collected and recycled and it requires less space underneath the
base, but it leads to increased consumption of electric power and
does not prevent the drawbacks noted in the first solution. Since
part of the cooling system operates at negative pressure, it is
susceptible to air intake which deteriorates the atmosphere and
oxidizes the load.
The third arrangement has the advantage over the others that all
the circulating gas passes through the coils, but these have the
drawback that given the space available, which is restricted, the
size of the coils is limited.
On the other hand, the stated coils are subjected to the furnace
operating temperature, approximately 700.degree. C throughout the
heating and annealing period, so that when the cooling stage is
reached, cold water is caused to circulate through the pipes. This
creates a heavy thermal shock which can be the cause of accidents
but, above all, it reduces the life of same. Further, coils located
in the current, within the diffuser of the bases, constitute
serious obstacles to gas circulation, with a resultant loss of
yield.
The arrangement of the present invention obviates the drawbacks of
these prior procedures and constitutes a simple and effective
assembly.
BRIEF DESCRIPTION OF THE DRAWINGS
For a better understanding of the system of the invention,
reference will be made to the following detailed description taken
with the accompanying drawings wherein:
FIG. 1 is a sectional view of bell furnace in which components
constituting the new cooling system are installed. The axis of
symmetry of the drawing divides the figure into two parts:
The right half shows the gas circulation circuit during the heating
phase and annealing of the load, and the left half shows the system
during cooling phase.
FIG. 2 is a Schematic plan view of the diffuser and valve
arrangement of the system of the present invention.
FIG. 2a is a perspective sectional view of the device taken
approximately from the circular area of FIG. 2.
DETAILED DESCRIPTION OF PREFERRED EMBODIMENT OF THE INVENTION
The furnace and cooling system of the invention is organized in the
following manner:
A cooling chamber (11) is situated at the base of the furnace,
between the metal base (15) of the furnace and a refractory hearth
of lining (4) having a suitable insulating capacity. A water cooled
coil (6) is installed in this chamber. Other complementary cooling
tubes (12) are welded to the metal base (15) exteriorly of chamber
11. A series of a suitable number such as eight collecting valves
(2) are arranged closely near the periphery of a centrally
positioned ventilator fan (1). The valves 2 extend through aligned
openings in hearth 4 and a diffuser 3 positioned immediately
thereabove. The valves 2 have cut-out portions forming gas
collecting surfaces 2' facing the periphery of fan 1. The valves 2
can selectively be moved to an open (ascend) position or to a
closed (descend) position by means of the activating mechanism (5).
When the valves ascend or open, gas impelled by the ventilator fan
(1) is intercepted by surfaces 2' of the valves and passes through
the valves to the chamber (11) where it loses heat. The cooled gas
returns to the load area of the furnace through the annular space
11' between the chamber (11) and the protective bell (9).
The location of the collecting valves closely adjacent the
ventilator fan periphery is a fundamental feature of the invention
to insure that the gas will reach the valves with the greatest
speed, thus necessitating its passage through only a small area.
The most desirable arrangement for the diffuser 3 is to have the
vanes or dividers thereof for channeling the gas alternately extend
to the ventilator fan periphery, the other vanes being shorter and
interrupted by valves 2. This arrangement is schematically
illustrated in FIG. 2. This is similar to American Rolec-type
distributors.
Performance of the furnace in its two phases of heating and cooling
is as follows:
During the heating and annealing phase (the right section of FIG.
1), the heating means such as resistors (14) situated on the
heating bell (13) radiate heat to the protective bell (9). Arrows
indicate that air impelled by the ventilator (1) passes through the
diffuser (3) and is deflected upwardly by the guide plate 3'
thereof into the space between the load 8 and bell 9 and is heated
on its vertical course by contact with the protective bell. The
thus heated gas enter convectors (10), communicating its heat to
load (8) and then descends through the inner space centrally of the
annular shape coils of the load 8, finally returning to the fan (1)
to reinitiate the cycle. During this entire phase the collecting
valves (2) have remained in their closed or lowered position.
When annealing, the circulating cycle of which has been stated, is
finalized, the load cooling stage as shown in the left part of FIG.
1 commences, it consisting of the following steps:
In the first place, naturally, the heating bell (13) is removed and
the collecting valves (2) are raised. Consequently, gas impelled by
the ventilator fan (1) is collected or intercepted by the surface
2' of the open valves and passes through the valves to the lower
cooling chamber (11) where it is guided by deflectors (not shown)
through a coil (6) and cooled thereby. The gas also losing heat by
contact with the lower base (15) which is cooled by water pipes
(12) welded thereto. The gas which has given off part of its heat
as it passes through chamber (11), exits by space 11' into the
space surrounding load 8 and takes heat from the load, thereafter
following the same path as during the heating cycle, to reenter the
fan, and then pass again to the chamber (11) to lose additional
thermal energy.
The basic advantages of this installation for cooling gas in a
closed circuit in bell furnaces can be summarized by the following
points:
1. Gas collection or interception by means of the valves 2 can be
effected due to the type of diffuser utilized in all gas
distribution canals in such a way that, despite losses through
joints, 100 percent of the circulating gas can be diverted and made
to pass through the cooler. Even considering the joint losses, more
than 80 percent of the gas can be diverted to the cooler.
2. By activating greater or fewer of the valves it is possible to
control the amount of diverted gas in as many ways as there are
valves. Consequently cooling speed may also be controlled.
It is likewise possible to open the valves to a greater or lesser
extent, thus causing the aforesaid control to be continuous.
3. As noted in FIG. 1, when the valves are closed there is nothing
to hamper free circulation in the base. Thus there is no
interference with the operation of the furnace during the heating
period or when annealing is in progress.
4. The coil and complementary cooling system are maintained with
water during the entire procedure, only the flow varying in
accordance with the need. In this manner the thermal shock so
detrimental to the life span of the cooling pipes is avoided.
5. Use of very modern refractory and insulating materials in the
construction of the bases offers a new perspective for the system.
It is thereby possible to reduce by 50 percent the conventional
thickness of the refractory lining and insulation of the base,
whereby it is possible to mount a fully refrigerated base having
the same thickness as present non refrigerated bases. It is
consequently possible to modernize existing plants at minimum cost
since construction work such as foundations, basements, etc., is
not necessary, nor is it required to change the essential
components of the furnaces since neither the course of the bells
nor the constitution of the bases vary. Modernization is then
restricted to replacing the base lining with a new one in addition
to the refrigerating components which can occupy exactly the same
space.
6. A detailed mathematical study of load losses occurring in the
two heating-annealing and cooling phases show that it is easy to
proportion the various components of the systems in such a way that
pressure losses may be exactly the same in both directions, whereby
operating conditions of the motor-ventilator unit are maintained
with optimum results.
* * * * *