U.S. patent number 3,793,867 [Application Number 05/258,722] was granted by the patent office on 1974-02-26 for apparatus for continuously quenching a heated metal plate.
Invention is credited to Franklin C. Safford.
United States Patent |
3,793,867 |
Safford |
February 26, 1974 |
**Please see images for:
( Certificate of Correction ) ** |
APPARATUS FOR CONTINUOUSLY QUENCHING A HEATED METAL PLATE
Abstract
An apparatus for continuously quenching a heated metal plate
moving and restrained in a plane. A pair of quench headers are
positioned above and below the plate each having a slot through
which quench fluid is directed at an angle in the direction of
plate movement. Beyond the impingement of the quench fluid on the
plate are a pair of sral grooved rollers positioned and spaced
apart engaging the top and bottom surfaces of the metal plate.
Inventors: |
Safford; Franklin C.
(Bethayres, Huntingdon Valley, PA) |
Family
ID: |
26878356 |
Appl.
No.: |
05/258,722 |
Filed: |
June 1, 1972 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
|
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182724 |
Sep 22, 1971 |
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Current U.S.
Class: |
72/201 |
Current CPC
Class: |
C21D
1/667 (20130101); B21B 45/0218 (20130101) |
Current International
Class: |
C21D
1/62 (20060101); C21D 1/667 (20060101); B21B
45/02 (20060101); B21b 027/10 (); B21b
045/02 () |
Field of
Search: |
;72/39,43,45,200-202,342
;29/121A,121H ;80/2,41 ;134/15,32,63,64
;148/20.6,125,143,145,146,152,153 ;239/107,506,513
;266/4S,5S,6S |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Lanham; Charles W.
Assistant Examiner: Combs; E. M.
Attorney, Agent or Firm: Beck; Paul A.
Parent Case Text
This application is a continuation-in-part of my copending
application Ser. No. 182,724 filed Sept. 22, 1971 for which I am
claiming the benefit of the filing date.
This invention relates to an apparatus for continuously quenching a
heated metal plate moving and restrained in a plane.
More particularly, this invention pertains to apparatus in which a
pair of slotted quench headers direct quench fluid at an angle in
the direction of movement of the plate which is subsequently
restrained by a pair of spiraled grooved rollers engaging the plate
on the top and bottom surfaces.
This invention represents an improvement over the structure shown
in my U.S. Pat. No. 3,420,083 (issued Jan. 7, 1969). That patent
discloses the use of grooved rolls whereas my present invention
teaches replacing those grooved rolls with spiral grooved rolls
having sloped walls forming the grooves. These rolls are used to
restrain the plate during the quenching operation. In using the
type of invention disclosed in my U.S. Pat. No. 3,420,083, large
quantities of water are delivered to the plate surface at a high
velocity. At the point of initial impingement, the angle must be
such as to assure the prevention of any water being driven back
along the plate surface in a direction opposite to that of the
plate advance. In working with such quantities of water and
pressures there is an accumulation of fluid on the top surface of
the plate, especially wide plate and the only route of escape is at
the edge of the plate. While the use of grooved rolls shown in my
U.S. Pat. No. 3,420,083 makes it possible for water to pass further
down the plate away from the area of initial impingement, it does
nothing to accelerate the movement of the water to the edge of the
plate. Furthermore, with straight or annular grooves there is at
the lines of contact, an interruption of the quenching fluid along
the plate surface following initial impingement. This could create
a condition whereby beyond those lines of interruption, the
subsurface heat of the plate raises the surface of the steel above
a temperature which will temper the steel at the surface causing a
loss of hardness and related properties. The steel gives evidence
of being tempered by having a typical bluish coloration. Though the
grooved roll shown in U.S. Pat. NO. 98 3,420,083 has only a limited
contact with the plate surface, this contact between roll and plate
does stop the quench water at the line of contact so that there is
no quench water in contact with the plate thereafter until water
from adjoining areas can flow into the dry areas. The result may be
stripes of soft steel on the plate surface which is surface steel
that has been tempered by the subsurface heat. To overcome these
problems I have designed a spiral grooved roller with sloped wall
grooves. The roller is spiraled from the center toward each end of
the roll. Water striking the walls of the grooves will then be
deflected toward the plate areas downstream to the lines of
interruption thereby bringing quench water quickly back into those
areas where the flow of water was interrupted by the intermittant
contact of the spiraled roll with the plate. This is of great
importance on the undersurface of the plate since the flow due to
gravity will not bring the water back into the areas which are dry
due to the interruption of the quench fluid by the spiraled roll
contacting the plate. There is an additional component of water
directed toward the plate surface as a result of the walls of the
grooves on the rolls being sloped. It is understood that these
spiraled grooves will convey plate accurately in the direction of
rotation so long as the plate rolls between the spiraled rolls and
does not slip in relation to the spiraled rolls.
Practical considerations in the past required an initial quench
water velocity of 150 feet per second to produce a perpendicular
velocity component of 30 ft./sec. at impingement with the metal
plate. This required water pressure at release of around 150 p.s.i.
The principal problem encountered in using the means directing
quench fluid in the equipment shown in U.S. Pat. No. 3,420,083 was
that it was necessary to release the water to atmosphere about 8
inches from the plate surface. Following its release the wter swept
around a curved deflector to direct it correctly to the required
point of impingement to effect the creation of a uniform curtain of
water. Obviously during the time the water traveled from point of
release to point of impingement a considerable decrease in velocity
occurred due to an unavoidable angle of water divergence,
entrainment of air and friction with the deflector. Such a decrease
in velocity and widening of the band of impingement considerably
reduces the severity of the resulting quench.
In present practices to avoid surface tempering, the plate is moved
at a relatively slow speed to allow time to elapse before the point
of water interruption. This results in plate warping between the
points of restraint before and after impingement of the quench
fluid and cooling of the plate to such a degree that the warpage is
fixed. Spiral grooved rolls permits higher plate speeds through the
quench with a considerable improvement in plate flatness. Actual
maximum speeds were originally 30 to 40 feet per minute for the
thinnest plate. The speed was then increased to 60 feet per minute
with the use of annular grooves. When using spiral grooved rolls,
the speed is no longer limited by the occurrence of surface
tempering caused by the interruption of flow of quench fluid along
the plate. Therefore, plate 3/16 inch thick can be passed through
the quench at speeds over 250 feet per minute. New techniques in
quenching use the heat remaining in the plate after rolling. Such
an operation requires higher plate speeds through the quench. The
one problem is that heavy plate takes less time to roll and more
time to quench. The solution is to quench at higher plate speed
which is made possible by the spiral grooved roll.
The invention of the new header makes it possible to release the
water at a point about 2 inches from the point of impingement. No
deflector is required to change individual jets to a curtain
because the fluid is in the form of a curtain at the point of
release. As a result it is possible to produce a nearrow band of
impingement fluid with a high perpendicular velocity component with
only about 40 p.s.i. water pressure at the point of release. This
effects a sharper and more effective band of impingement with very
substantially reduced requirements for volume and pressure of
quench water. This means a considerable saving of money in water
supply facilities with comparable savings in power requirements for
average size plate quenches.
I provide an apparatus for continuously quenching a heated metal
plate moving and restrained in a plane, the improvement comprising
means applying a curtain of quench fluid which impinges the top and
bottom surfaces of the metal plate; the fluid is applied in the
direction of movement of the metal plate; and a pair of spiral
grooved rollers positioned and spaced apart to engage the top and
bottom surfaces of the metal plate, the rollers are positioned
subsequent to the impingement of the quench fluid in the direction
of movement of the metal plate.
I preferably provide that the spiral grooved rollers are formed by
sloped walls and the spiral going from the center to each end of
the roll.
I preferably provide that the means applying a curtain of quench
fluid comprises a pair of corresponding headers positioned above
and below the travel of the metal plate, each header formed by a
gate member converging with a rigid back member to form a
longitudinal slit across the path of the plate travel, the slit
oriented to face the plate at an angle in the same direction of
travel of the metal plate, the gate member is adjustable to vary
the opening of the slit and means supplying quench fluid to each
header.
Other objects, purposes and advantages of the invention will become
apparent as the following description of a present preferred method
of practicing the invention proceeds.
Claims
I claim:
1. Apparatus for continuously quenching a heated metal plate moving
and restrained in a plane, the improvement comprising:
a. header means for impinging a continuous curtain of quench fluid
on the top and bottom surfaces of the metal plate, the curtain of
quench fluid being applied in the direction of movement of and at
an acute angle with respect to the metal plate; and
b. a pair of parallel spirally grooved rollers positioned and
spaced apart to engage the top and bottom surfaces of the metal
plate, the rollers being positioned downstream with respect to the
line of impingement of the quench fluid in the direction of
movement of the metal plate, and effective to distribute the
quenching fluid uniformly and evenly over top and bottom surfaces
of the moving plate as it moves past said rollers.
2. Apparatus as recited in claim 1 wherein the spirally grooved
rollers have grooves formed by tapered rib walls which slope
inwardly as the height of the walls approaches the outer surface of
the roller.
3. Apparatus as recited in claim 1 wherein each of said header
means is formed by a hinged gate member releasably fixed in a
converging position with respect to a rigid back member to form
therewith a longitudinal slit across the path of the plate travel,
the slit being oriented to direct the curtain of quench fluid in
the direction of travel of the metal plate and at an angle of
10.degree. to 40.degree. thereto, the gate member being adjustable
in length to vary the width of the opening of the slit, and conduit
means supplying pressurized quench fluid to each of said header
means.
4. Apparatus as recited in claim 1 wherein each of the spirally
grooved rollers comprises a shaft and a plurality of discrete
spirally grooved cylindrical segments which are mounted in spaced
relation along said shaft, the segments to one side of the
longitudinal center of each roller having grooves spiraled in one
direction and those on the opposite side of the longitudinal center
of the roller having grooves spiraled in the opposite
direction.
5. Apparatus as recited in claim 1 wherein each of said header
means is formed by a gate member having a pivot connection at one
end to a rigid back member and converging with the rigid back
member at an end opposite the pivot connection to form with the
back member a longitudinal slit across the path of the plate
travel, the slit being oriented to direct the curtain of quench
fluid in the direction of travel of the metal plate, and means for
holding the gate in a fixed position and for moving it pivotally
toward and away from the rigid back member to vary the width of the
opening of the slit to enable accumulated obstructions therein to
be flushed out by pressurized fluid supplied to the header
means.
6. Apparatus as recited in claim 2 wherein the tapered rib walls of
the spirally grooved rollers extend in opposite directions from the
center of the roller toward each end, the oppositely extending
sections of said tapered rib walls meeting in end-to-end abutting
relation at the center of the roller.
7. Apparatus as recited in claim 5 wherein the rigid back member is
U-shaped in cross-section and wherein the means for moving the gate
member pivotally toward and away from the rigid U-shaped back
member comprises a rod connecting the rigid U-shaped back member
and the gate member, the rod extending through an opening in the
gate member and having threads on the end of which a corresponding
nut is screwed which when turned in one direction allows the gate
member to be pivoted away from the U-shaped back member by the
pressurized fluid within the header means and which when turned in
the opposite direction moves the gate member toward the U-shaped
back member.
8. Apparatus as recited in claim 7 wherein a resilient biasing
means is inserted on the rod between the gate member and the nut
for yieldingly holding the gate member in position against the
force of pressurized fluid within the header means.
9. Apparatus as recited in claim 1 wherein each of said header
means is formed by a hinged gate member releasably fixed in a
converging position with respect to a rigid back member to form
therewith a longitudinal slit acorss the path of the plate travel,
the slit being oriented to direct the curtain of quench fluid in
the direction of travel of the metal plate and at an angle of
10.degree. to 40.degree. thereto, and conduit means supplying
pressurized quench fluid to each of said header means.
Description
In the accompanying drawings I have illustrated a present preferred
method of practicing the invention in which:
FIG. 1 is a longitudinal sectional view of the quench
apparatus;
FIG. 2 is an isometric portion of the quench apparatus including
the quench headers 18 and 20 with a pair of spiraled grooved rolls
and a subsequent pair of quench spray pipes showing a plate
traveling between the pairs of headers and rolls;
FIG. 3 is an elevational view of a spiraled grooved roll;
FIG. 4 is a cross sectional view of the roll shown in FIg. 3 and
taken on the line IV--IV of FIG. 3;
FIG. 5 is an enlarged fragmentary view of one of the quench
headers;
FIG. 6 is an elevational view of another embodiment of a spiraled
grooved roll which can be used instead of the spiral grooved roll
shown in FIG. 3;
FIG. 7 is another embodiment of an enlarged fragmentary view of a
quench header which can be used instead of the header shown in
FIGS. 2 and 5; and
FIG. 8 is an elevational view of another embodiment of the threaded
rod and nut at the gate of the header shown in FIG. 7.
Referring to FIG. 1, the apparatus comprises a plurality of upper
and lower entry cylindrical rolls 10, 12, 14 and 16 which restrain
the plate 30 in a plane at the entry end 26 of the apparatus.
Adjacent to rolls 12 and 16 are top and bottom quench headers 18
and 20 which produce high velocity quench curtains (sheets of
liquid) 62 and 64 respectively which impinge the metal plate 30 on
top and bottom surfaces of the plate. Positioned beyond quench
headers 18 and 20 in point of travel of the plate 30 are spiraled
grooved rolls 22 and 24 engaging the top and bottom of the plate 30
followed by quench spray pipes 32 and 34 which supply quench fluid
on the plate 30 and toward rolls 22, 24, 36 and 38. Positioned
beyond quench spray pipes 32 and 34 are additional spiraled grooved
rolls 36 and 38 which engage the top and bottom of the plate 30.
Positioned beyond those rolls are quench spray pipes 40 and 42 and
additional spiraled grooved rolls 44 and 46.
As plate 30 leaves a furnace it enters into the entry end of the
apparatus described where it is restrained in a plane by the entry
rollers and the spiraled grooved rollers until it leaves at the
exit end of the apparatus. The main headers 48, 50, 52 and 54
supply quench headers 18 and 20 and quench spray pipes 32, 34, 40
and 42 with quench fluid. The quench spray popes 32, 34, 40 and 42
have a plurality of openings (or nozzles) to release the quench
fluid. Beams 58 support the spiraled grooved rolls 22, 24, 36, 38,
44 and 46. Frames 60 and 61 support the support beams 58 and rolls
10, 12, 14 and 16 as well as headers 18 and 20 and the quench spray
pipes 32, 34, 40 and 42. The upper rolls have a load 56 exerting a
downward force which is transmitted to the plate 30. All of the
cylindrical rolls and the grooved rolls 10, 12, 14, 16, 22, 24, 36,
38, 44 and 46 are driven at the same speed by means of a sprocket
and chain motor drive shown in my earlier U.S. Pat. No. 3,423,254.
Rolls 10, 12, 22, 36 and 44 rotate in the opposite direction from
rolls 14, 16, 24, 38 and 46. Each of the rolls are journaled and
supported by bearings as shown in my U.S. Pat. No. 3,423,254. The
upper frame 60 is pre-positioned until the top cylindrical rolls 10
are positioned to restrain the metal plate 30 as it enters the
apparatus after leaving a furnace. The metal plate 30 then passes
between rolls 12, 16, 22, 24, 36, 38, 44 and 46. Quench fluid 62
and 64 in the form of a continuous high velocity curtain impinges
the metal plate 30 which sets the cooling temperature of the metal
plate 30. The high velocity quench curtains impinge the plate 30 on
top and bottom surfaces at an angle between 10.degree. and
40.degree. which prevents the quench fluid from reaching a part of
the work 30 which has not advanced to the point of impingement.
FIG. 2 shows a more detailed isometric view of the headers 18 and
20 which provide the initial quench curtains 62 and 64 with the use
of the spiraled grooved rolls 22, 24, 36 and 38 with additional
quenching spray pipes 32 and 34. All of the spiraled grooved rolls
22, 24, 36, 38, 44 and 46 are identical. Rolls 44 and 46 are not
shown in FIG. 2. The spiraled grooved roll 22 (also shown in FIGS.
3 and 4) shows a plurality of spiraled rib-like walls 74 disposed
in parallel spaced relation, the walls extending from the center 76
in opposite directions outwardly to each end 78 and 80 (shown also
in FIG. 3). The spiraled walls are tapered symmetrically in
thickness, that is the side surfaces 82 and 84 slope inwardly as
the wall approaches the outer surface of the roll 22 (shown in FIG.
4). The use of the spirally grooved roll 22 with the spiraled walls
74 directed from the center 76 toward each end 78 and 80
accelerates the movement of the quench fluid to the edge of the
plate 30. Quench fluid is also deflected toward the plate areas
downstream in the line of travel of the plate to the points of
interruption thereby bringing quench liquid quickly into those
areas where the flow of quench fluid was interrupted by the
intermittent contact of the spirally grooved roll. The sloped sides
of the walls provide an additional component of quench fluid
directed toward the plate surface.
FIGS. 2 and 5 show detailed isometric views of the headers 18 and
20. The header 18 is coupled to the main header 48 by the conduit
coupling 86 shown in FIG. 5. Headers 18 and 20 are identical except
they are reversed in position and are positioned directly above and
below and facing each other allowing the plate to pass between
them. Header 18 has a gate member 88 which converges with a rigid
back member 90 to form a longitudinal slit 92 across the path of
the plate 30 travel. The slit 92 is oriented to face the plate 30
at an angle in the same direction of the travel of the metal plate
30. Gate member 88 is adjustable to vary the opening of the
longitudinal slit 92 by loosening bolts 94 and 96 which are
inserted through oversized holes. The gate member 88 can be moved
upwardly or downwardly to vary the slit opening 92. A hinge member
98 couples the gate member 88 and can be swung open after bolt 94
is removed for ease of cleaning obstructions from the slot and
replacemnt of gate member 88.
After the initial line of impingement 100 on plate 30 (FIG. 2) is
formed by quench curtains 62 and 64, quench spray pipes 32, 34, 40
and 42 provide quench fluid on the plate 30 toward each of the
spiraled grooved rolls that the particular quench spray pipe
straddles.
The initial quench fluid in the form of quench curtains 62 and 64
impinge the metal plate 30 at a high velocity which sets the
cooling temperature of the plate 30. The quench fluid then travels
between the spiraled grooved rolls 22, 24, 36, 38, 44 and 46 and
follows the metal plate 30 which is restrained by the rolls. The
additional quench fluid from quench spray pipes 32, 34, 40 and 42
maintains the cool temperature reached at the initial impingement
point 100 (FIG. 2) on the plate 30 surface.
The spiral grooved rolls 22, 24 shown in FIGS. 2 and 3 are
expensive to make and machine. To provide a spiral grooved roll at
a reduced cost the spiral grooved roll generally shown as 102 in
FIG. 6 was developed. It comprises a shaft 104 on which are mounted
a plurality of discrete cylindrical spiral segments 106 and 108.
The segments 106 have their spiral grooves oriented in reverse
direction of the cylindrical spiral groove segments 108. The
segments are divided in their orientation at the center 110 of the
shaft 104. The use of the segments gives the advantage of being
able to use segments which can be cut on machines for cutting worms
or they can be cut on a suitable gear cutting machine. By using
segments made from gear cutting machines the cost of producing the
spiral groove rolls is greatly reduced.
FIG. 7 shows another embodiment of a header 112. The purpose of the
header 112 is to provide an adjustable opening to quickly and
easily flush out accumulated obstructions. The header 112 comprises
a U-shaped, rigid back member 114 and a gate 116 which is pivotally
connected at 118 by means of a hinge 120 on one end of the gate
member 116 and a corresponding end of the U-shaped rigid back
member 114. The other end of the gate member 116 opposite the pivot
118 converges with the U-shaped rigid back member 114 to form a
longitudinal slit 122 across the path of the plate travel. The slit
is oriented to face the plate at an angle in the same direction of
travel of the metal plate. To open the gate member 116 a rod 124
extends through both the gate member 116 and U-shaped rigid back
member 114. It is threaded at each end and has corresponding nuts
126 and 128. Rubber gaskets 130 and 132 hold leakage through gate
and the rigid U-shaped back member to a minimum. In order to move
the gate 116 away from the rigid backup member 114 about pivot 118
and thereby open the slot 122, nut 128 is rotated. This enables one
to flush out any accumlated obstructions. For a very long header,
there would be a plurality of rods 124 with corresponding nuts 128
and each of the nuts would be coupled to an output shaft of a small
worm gear reducer. The reducers would all be in a line and would
have their inward shafts all coupled together in series. In this
manner all the adjusting nuts could be turned simultaneously and
uniformly by rotating the coupled input shafts either manually or
by a suitable powered unit. The slot 122 would then be opened or
closed through its full length for flushing or for adjustment of
the slot width.
FIG. 8 shows a resilient biasing means 134 between the gate member
116 and the nut 128 on the rod 124.
* * * * *