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AU624575B2 - Coolant flow control - Google Patents

Coolant flow control Download PDF

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AU624575B2
AU624575B2 AU18005/88A AU1800588A AU624575B2 AU 624575 B2 AU624575 B2 AU 624575B2 AU 18005/88 A AU18005/88 A AU 18005/88A AU 1800588 A AU1800588 A AU 1800588A AU 624575 B2 AU624575 B2 AU 624575B2
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flow
roll
coolant
control
work piece
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AU1800588A (en
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William John Edwards
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Description

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U,,
PCT
AU-AI-18005/88 WORLD INTELLECTUAL PROPERTY ORGANIZATION International Bureau a INTERNATIONAL APPLICATION EBL EN I T PAJT COOPERTIONTREATY (PCT) 'N&L 4, N T _PA_EVT COOPERATION TREATY (PCT) (51) International Patent Classification 4 (11 ntern tionalllication Number: WO 88/ 09230 B21B 27/10, B23Q 11/10 Al (43) International Publication Date: 1 December 1988 (01.12.88) (21) International Application Number: PCT/AU88/00156 (22) International Filing Date: 24 May 1988 (24.05 Published With international search report.
(31) Priority Application Number: (32) Priority Date: (33) Priority Country: PI 2206 28 May 1987 (28.05.87) (71)(72) Applicant and Inventor: EDWARDS, William, John [AU/AU]; 1 Jabiru Road, Carey Bay, NSW 2283
(AU).
(74) Agent: SHELSTON WATERS; 55 Clarence Street, Sydney, NSW 2000 (AU).
(81) Designated States: AT (European patent), AU, BE (European patent), CH (European patent), DE (European patent), FR (European patent), GB (European patent), IT (European patent), JP, LU (European patent), NL (European patent), SE (European patent),
US.
A.O.J.P. 23 FEB 1989
AUSTRALIAN
2 1 DEC 1988 PATENT OFFICE i i i i i ,i i a i 1 i -i
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(54) Title: COOLANT FLOW CONTROL (57) Abstract A method and apparatus for controlling the temperature of a machine tool mill rolls A coolant or lubricant is fed from a header supply (22) to the primary inlet (21) of a fluidic device (20) such as a vor- 36 tex valve. The outlet (23) of the fluidic device (20) is di- 34 rected to or at the machine tool A second flow (36) of coolant or lubricant from reservoir (25) is fed to the control inlet (30) of the fluidic device (20) the sec- 33 ond flow (36) being controlled via a feedback signal /22 (27) and valve (26) to vary the second flow (36) in re- sponse to workpiece shape or temperature so that the total outflow from the outlet (23) of coolant or lubricant can be varied. The second flow (36) may be at a temperature which differs from that of the first flow so that as the flow rate from outlet (23) to the workpiece 27 rises the temperature of the coolant or lubricant falls. 26 1 I -41i .a rii ii 1 1$ WO 88/09230 PCT/AU88/00156 1 TITLE: COOLANT FLOW CONTROL FIELD OF THE INVENTION The present invention relates to means for supplying a coolant or lubricant to a tool or a work piece.
The invention is applicable for supply of a coolant or lubricant to a mill roll.
SThe term "tool" is used broadly in this specification to include a mill roll as well as machine Stools and the term work piece includes ingots, strip and other forms of workpiece.
BACKGROUND ART In rolling mills such as are used for production of high quality rolled flat metal strip, any variation in temperature over a work roll surface may cause differential radial expansion of the mill roll, referred S2 1_1__1_ i f i :t -i i i i ::i i
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i t!; i WO 88/09230 PCT/AU88/00156 2 to as thermal camber, and thus result in transverse variations in thickness and flatness of the rolled product. Control of strip flatness (shape) requires maintenance of mill roll thermal camber within close tolerances.
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Variations in the transverse thickness profile during rolling may cause non-uniform lengths to be produced at different locations across the strip width and these result in a non-uniform transverse stress distribution which may cause buckling. When rolling under tension, the buckling usually does not occur and a shapemeter then measures the transverse stress variation which is interpreted as the tendency to subsequent buckling (or bad shape).
It is usual to provide at least one row of spray nozzles through which a coolant and/or lubricant is applied to the roll surface. Usually the nozzles are disposed in three or more transverse zones, the nozzles in each zone being supplied with fluid at a pressure which differs from each other zone. The flow rate of coolant through the pressure supplied to each zone of nozzles, or through each individual nozzle, is adjusted to control roll expansion and/or level of lubrication to suit the current rolling requirements. The latter depend in a complex manner upon mill loads, roll deflections and ground profiles, workpiece thickness and temperature profile and roll bending settings.
i-i 1 _i L i. WO 88/09230 PCT/AU88/00156 3 It has been practiced to locate a shape meter downstream of the mill roll and to use feedback signals indicative of strip shape variation to control thermal camber in the roll. The shape meter is adapted to measure variations in the transverse stress and/or temperature distribution in the product resulting from rolling, including the effect of mill roll distortion.
The measurements are made at a plurality of points in the product width direction. Each spray nozzle may then be provided with a separate valve and the shape meter may be used for generating feedback signals to control individual valves. Individual valves are controlled to provide a greater flow rate of coolant to parts of the mill roll or work piece which are excessively hot or have more radial expansion than is desirable. In this way, variations in thermal distortion and consequent variations in strip shape, may be minimized.
On-off control, rather than analogue control, of valves is often used to reduce the complexity oL communication interfaces between automation equipment and the valve actuators and to reduce valve costs, variable flow being achieved by use of multiple valves of different sizes in each zone and/or by varying the ratio of "on-time" to "off-time". Known systems for roll shape feedback control utilize a large number of electzic or pneumatically controlled valves which must be operable in an extremely hostile environment and are- -Ti 4 consequently each of costly construction. The valve nozzles are susceptible to blockage and because one blocked valve nozzle could result in roll overheating, it is usual to have a redundant set of "stand-by" valves and to stop the line if a severe blockage occurs.
An object of the present invention is the provision of means for supplying a coolant or lubricant to a mill roll or other tool or work piece which avoids at least some of the disadvantages of the prior art.
DISCLOSURE OF THE INVENTION According to a first aspect, the invention consists in a method for controlling the temperature of a work roll or work piece in a rolling mill, said method comprising the steps of: directing a first flow of a first cooiant or lubricant to a primary inlet of a vortex valve; directing a second flow of a second coolant or lubricant to a control inlet of the vortex valve, said second coolant or lubricant having a characteristic substantially different from that of said first coolant or lubricant; mixing the first flow with the second flow I within the vortex valve; conducting a mixed outflow from an outlet of the vortex valve to the work roll or work piece; and varying the flow rate of the second flow LA thereby to control the outflow conducted from the vortex valve to the roll or work piece in respect of bothflow rate and said characteristic.
A;t 42 lli 5 Preferably, said parameter is temperature, concentration or fluid pressure.
In preferred embodiments of the invention at least a portion of the spent coolant or lubricant after extraction of heat is recycled to the primary inlet.
According to a second aspect, the invention consists in a rolling mill for working a rolled product, oooo said mill comprising: *e e a vortex valve having a primary inlet, a control inlet, and an outlet; 0 means for directing a first flow of a first coolant or lubricant to the primary inlet; ee means for directing a second flow of a second 000* coolant or lubricant to the control inlet, said second coolant or lubricant having a characteristic substantially different from that of said first coolant or lubricant; **0e00 S" means for directing a mixed outflow from the outlet of the vortex valve to the roll or work piece; and means for varying the flow rate of the second flow thereby to control the outfldw conducted from the vortex valve to the roll or work piece in respect of both flow rate and said characteristic.
Where the fluid supplied to the primary inlet is at a different concentration from the fluid supplied to the control inlet, this enables a different concentration of lubricant to be used selectively on individual headers or, if required, for individual nozzles. The latter a, ~g~b~l44 7rE 5a facility has advantages in that it allows the edge regions of a hot strip rolling mill to be preferentially lubricated with major advantages in wear reduction and without excessive contamination of the coolant system by lubricant. Use of a vortex valve allows excellent mixing to be achieved and, at the same time, provides variable control over the concentration. A vortex valve may be used in the manner described to achieve effective mixing of rolling oils with a recirculating coolant system. A high pressure control flow should then be used to ensure maximum turbulence in the exit region of the vortex valve.
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C12o go WO 88/09230 PCT/AU88/00156 -6- Desirably, two valves are used at each location across the work roll of a rolling mill, one valve for selectively applying lubricant and the other valve to selectively apply coolant so as to control the roll expansion, thereby maintaining a more corstant strip thickness profile and reducing the amount of customary edge thickness tapering in the region up to 200 mm from the strip edge.
BRIEF DESCRIPTION OF DRAWINGS Various embodiments of the invention will now be described by way of example only with reference to Figures 1 to 5 wherein: Figure IA is a schematic plan view of a vortex valve for use in the invention. Figure IB shows the valve of Figure 1A in schematic elevation, Figure 2 is a graph useful for illustrating characteristics typical of a vortex valve such as shown in Figure 1 wherein exit flow is shown on the upright Saxis and control flow pressure is shown on the i horizontal axis, and Figure 3 is a schematic diagram of an embodiment of the invention.
Figures 4 and 5 show schematically a configuration which may optionally be used in the embodiment of Figure 3.
WO 88/09230 PCT/AU88/00156 -7- DESCRIPTION OF PREFERRED EMBODIMENTS With reference to Figure 1, there is shown a vortex valve comprising a generally cylindrical conical or frustro conical valve chamber 1 having a primary inlet 2 which is radially directed; a control inlet 3 which is tangentially directed in a direction transverse primary inlet 2; and having an outlet 4 which preferably extends in an axial direction.
In the absence of a flow through the control inlet 3, a primary flow admitted to valve chamber 1 via primary inlet 2 exits from outlet 4.
If a control flow is admitted through control inlet 3 at a high pressure in comparison with the primary flow, the exit flow from the outlet 4 is reduced.
Figure 2 is a graph showing total flow (L/min) on the vertical axis 5 and control pressure (kPa) on the horizontal axis 6 for a typical vortex valve operating with main supply pressure equal to 100 kPa. The vortex valve to which Figure 2 applies has a chamber 1 of 50 mm diameter, an inlet tube 2 of 12.5 mm diameter and a single entry control flow tube 3 of 2.6 mm diameter. As shown by the graph, the total flow at outlet 4 reduces as a function of increase in the control flow and approaches a minimum flow. Vortex valves per se are well known in many designs or configurations and require no further description.
With reference to Figure 3 there is shown 8 schematically one embodiment of the invention. The embodiment shows a stand of a strip mill having a top roll 7 and a bottom roll 8.
There is further provided a vortex valve 20 having a primary inlet 21 adapted to receive coolant from a header supply 22 via a primary flow pump 28.
The outlet 23 of valve 20 is adapted either to spray directly onto a mill roll 7 or preferably is conducted to a respective spray nozzle 24 directed at o roll 7.
*A second flow 36 of coolant is fed to control inlet ease 30 of vortex valve 20 by means of pump 29 from a secondary supply reservoir 25 at a flow rate which may be varied by means of a control valve 26 which is electrically or pneumatically operated by a respective P feedback control signal 27 from a shape meter (not shown i .in Figure 3) located downstream of the mill rolls. The shape meter generates a signal 27 indicative of a change S•in the flatness or stress distribution of rolled strip ,on a line in the strip rolling direction corresponding so*: with the position of nozzle 24 with respect to the mill K roll 7. In use feedback signal 27 operates control valve 26 to increase or decrease control flow from reservoir 25 to vortex valve control inlet 30. If the control flow 36 to valve inlet 30 increases, the total flow of coolant from that vortex valve outlet 23 to the mill roll 7 decreases.
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WO 88/09230 PCT/AU88/00156 9 In a preferred embodiment the control flow coolant Sat 30 is at a higher temperature than the primary flow coolant at 21.
Hot coolant which is spent after cooling the mill rolls is pumped from sump 40 by a pump 41 through a heat exchanger 31 whereby waste heat is extracted and the resultant cold coolant is returned via line 32 to header supply 22. A fraction of the hot coolant is taken off at 35 between pump 41 and heat exchanger 31, passed through a filter 33 and relieved via line 34 to secondary supply reservoir 25 from which the control flow emanates.
Consequently when the control flow into inlet 30 is at a maximum, the flow rate of coolant from outlet 23 is not only at a minimum but is at a maximum temperature, consisting predominantly of hot coolant. As the control flow of the hot fluid into inlet 30 is reduced the flow rate of cold coolant increases, the proportion of hot control flow in the outflowing mixture is reduced and the temperature of the outflow from outlet 23 falls.
The system thus utilizes both a change in flow rate, and a change in temperature of the coolant to control the roll temperature.
In practice a plurality of nozzles 24 are disposed in a row extending the width of the top roll and/or of the bottom roll.
Each nozzle of the plurality is in communication
K
10 with the outlet 23 of a corresponding one of a plurality of vortex valves 20. The control flow of each vortex valve 20 is varied by means of a corresponding respective control valve 26, or if desired a group of vortex valves 20, may be controlled by a shared control valve 26.
More than one nozzle 24 may be fed from a vortex valve.
Thus, for example, an upper and corresponding lower roll nozzle 24 may both be fed by one vortex valve outlet 23; or by separate vortex valves controlled by a eo *single control valve 26; or by separate vortex valves each under the control of a respective control valve 26.
The control valves may be of an analogue type controlled by signals from a shape meter or similar transducer or may be an on/off valve, the ratio of so "on-time" to "off-time" being influenced by the feed *0 back signals.
0 Similarly, if a traeisverse temperature distribution for the roll or rolled product is measured, instead of the strip shape, then it may be controlled in a similar manner to that described above for strip shape control.
'I Thus the control signal may be provided by a temperature transducer or other transducers For preference in case of maintenance, and to provide a better environment for the control valves, the S on-off control valves are located away from the headers 2,, f WO 88/09230 PCT/AU88/00156 .3 iiat the side of a mill. A pump provides a high pressure i3 supply of filtered control fluid with a common supply 4 being available to all stands. Typically about 10% of the total coolant flow is used for control. In some Sinstances, for example, if different fluid temperatures are involved, higher control flow fractions may be advantageous.
The control signal flows are preferably diverted by flexible armoured hydraulic cables provided with quick release couplings.
For preference the connection of fluid control Ssignals to individual vortex valves is accomplished by Smeans of a distribution disc located at one or both ends of each flexible control flow cable. This enables the number of control valves to b. minimised. It also allows the number of control signals in the flexible i cables to be minimised whilst maintaining a standard design of header in which each vortex valve is individually connected to the distribution disc at the i point where the control cable connects to the header.
The distribution discs have channels or grooves which provide an arbitrary connection between the inlet control po:rts and the outlet ports to the vortex valves.
Advantages of the system include that a greatly reduced number of control valves is required for a given degree of control since more than one spray nozzle can be controlled by each vortex valve and since less than
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-12 half the number of control valves is needed in comparison with conventional headers since rediindancy is I unnecessary.
The vortex valves may be adapted for automatic unblocking of valves and nozzles, for example by means of a counter flow and filter system involving the reduction of the primary supply pressure and increasing the control pressure to maximum. This c cause a reversal of the primary flow and unblocking of the inlet C, *e pipe or inlet filters on the primary supply.
The system is able to operate with low pressure valves and to use a standardized modular design for all widths of roll. The system has no moving parts and is less susceptible to blockage. A minilnum flow is guaranteed under all normal operating conditions.
:Surprisingly we have found that when the fluid from outlet 4 of a vortex valve is directed through a "V" slot or similarly shaped nozzle, the emanating spray may 0 be changed from fan-shaped spray envelope to a conical-shaped spray envelope depending on the control flow and other factors. This characteristics is controlled by varying the distance from the point where the outlet flow leaves the conical chamber to the spray nozzle. The longer the distance, the less rotational swirl remains in the flow at the spray nozzle and the less tendency there is to form a conical. shape of envelope ("conical spray"). This means that, when the i7 WO 88/09230 PCT/AU88/00156 13 K control flow is off, the fluid emerging from the nozzle will have a low angular momentum and little tendency to Iform a conical spray for the case of a jet.
However, when the control flow is applied, the spray characteristic will change to that of a conical spray.
This characteristic may be utilized in two ways.
Firstly, it may be used to generate conical-shaped sprays without the complexity and blockage tendencies of special-purpose nozzles of conventional design.
Secondly, by interposing a plate containing a carefully sized slot, between the nozzle and the roll or Tiorkpiece, additional flow rate variations are possible. This is achieved by locating the nozzle close Sto the vortex chamber exit to maximise the tendency to form a conical spray shape. Therefore, when the control i flow is at a maximum, the normally fan-shaped spray i i which passes through the slot when the control flow is off is converted to a conical spray which impinges on i the interposed plate and little, if any, flow goes to the-roll or workpiece. By this means, the effective control range of the roll cooling or lubricating device is effectively increased significantly.
With reference to Figure 4 and Figure 5 a shield or plate 40 defining a slotted apperture 42 is shown with impinging sprays from a jet nozzle 41 for the cases of control flow on (Figure and control flow off (Figure Figure 4 shows how with control flow to i WO 88/09230 PCT/AU88/00156 i:.
14 valve 20 off a major proportion of the fan-shaped spray passes through slot 42 and impinges on roll 7. In Figure 5, the control flow to valve 20 is the spray is conical and the major proportion of the conical-shaped spray is unable to pass through the i' narrow rectangular slot 42.
The use of conical spray shapes and associated, modified coolant droplet characteristics also alters the heat transfer coefficient between the coolant and the roll and may be used to advantage in particular applications of the technology.
Because vortex valves store angular momentum when i the control flow is "on" the valve has "inertia" and ;Y thus a lower frequency pulse rate may be used when Sachieving modulated flow with a defined on-time and off-time ratio.
Although the invention has herein been described K with particular reference to vortex valves, other suitable fluidic valves having an equivalent operation may be substituted therefor.
SAs will be apparent to those skilled in.the art from the teaching hereof, the invention may be applied in other embodiments and in other forms without departing from the concept hereof and such embodiments or forms are deemed to be within the scope hereof.
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Claims (19)

1. A method for controlling the temperature of a work t roll or work piece in a rolling mill, said method comprising the steps of: directing a first flow of a first coolant or r lubricant to a primary inlet of a vortex valve; s directing a second flow of a second coolant Bo•. or lubricant to a control inlet of the vortex O* 7 valve, said second coolant or lubricant having a Sr characteristic substantially different from that of said first coolant or lubricant; mixing the first flow with the second flow within the vortex valve; conducting a mixed outflow from an outlet of is: the vortex valve to the work roll or work piece; and varying the flow rate of the second flow 9 Sthereby to control the outflow conducted from the i *mwi vortex valve to the roll or work piece in respect of both flow rate and said characteristic.
2. A method according to claim 1, wherein said tW1 characteristic is temperature. .SE
3. A method according to claim 1, wherein said characteristic is concentration.
4. A method according to claim wherein said p! 1] characteristic is fluid pressure. cl A method according to claim 1, including the OU IL further steps of: monitoring a variable parameter of the Swork piece during rolling; generating a control IN -16 signal indicative of variations in said parameter; and controlling the flow rate of the second flow in response t~o said control signal to compensate for variations in said parameter.
6. A method according to claim 5, wherein the flow rate of the second flow is controlled in response to a signal indicative of a change in flatness of the work piece during rolling.
7. A method according to claim 5, wherein the flow rate of the second flow is controlled in response to a fe 0 fees 0signal indicative of a change in temperature of the work piece during rolling.
08. A method according to claim 5, wherein the flow rate of the second flow is controlled in response to a signal indicative of a change in stress distribution of the work piece during rolling.
9. A method according to any one of claims 1 to 8, wherein at least a portion of spent coolant or lubricant is recycled to the primary inlet of the vortex valve. A method according to any one of claims 1 to 9, wherein two vortex valves are used, one of said valves son: as 0 selectively supplying lubricant and the other of said valves selec 'ively supplying coolant to the roll or work piece.
11. A method according to any one of the preceding claims, further including the step of directing the outflow through a nozzle and controlling the shape of CD, UjN r 17 spray envelope emanating from the nozzle by varying the second control flow into said vortex valve.
12. A method according to claim 11, including the further step of interposing an apertured shield intermediate the nozzle and the roll or work piece, said shield permitting a relatively high proportion of the ic spray to pass through the aperture in one configuration ose of spray envelope and a relatively low proportion of the spray to pass in another configuration of spray envelope ooooo S• thereby to provide an additional degree of control over the outflow reaching the roll or work piece.
13. A method for controlling the temperature of a work roll or work piece in a rolling mill, said method being 0e 0 substantially as hereinbefore described with reference to Figure 3 or Figures 4 and 5 of the accompanying drawings.
14. A rolling mill for working a rolled product, said o 0.0. mill comprising: a vortex valve having a primary inlet, a control inlet, and an outlet; means for directing a first flow of a first coolant or lubricant to the primary inlet; means for directing a second flow of a second coolant or lubricant to the control inlet, said second coolant or lubricant having a characteristic substantially different from that of said first coolant or lubricant; ALI 1 means for directing a mixed outflow from the outlet r 18 of the vortex valve to the roll or work piece; and means for varying the flow rate of the second flow thereby to control the outflow conducted from the vortex valve to the roll or work piece in respect of both flow rate and said characteristic. A rolling mill according to claim 14 wherein said characteristic is temperature.
16. A rolling mill according to claim 14 wherein said characteristic is concentration.
17. A rolling mill according to claim 14 wherein said o: characteristic is fluid pressure. CCCS
18. A rolling mill according to any one of claims 14 to c17, further including means for monitoring a variable S0 parameter of the work piece during rolling, means for generating a control signal indicative of variations in said parameter, and means for controlling the flow rate 0o, of the second flow in response to said control signal to I •compensate for variations in said parameter. be CC 0"19. A rolling mill according to claim 18, further including a shape meter to generate a control signal I indicative of change in flatness or stress distribution I of the rolled product and wherein the flow rate of the B second flow is controlled in response to that signal. A rolling mill according to any one of claims 14 to 19 further including means to recycle a portion of spent coolant or lubricant to the primary inlet of the vortex valve. q ,L 19
21. A rolling mill according to any one of claims 14 to wherein two said vortex valves are used, one of said valves selectively applying lubricant and the other of said valves selectively applying coolant to the roll or work piece.
22. A rolling mill according to any one of claims 14 to 21 further including nozzle means adapted to produce a spray envelope, the shape of which can be controlled by varying said control flow.
23. A rolling mill according to claim 22 further o including an apertured shield disposed intermediate the oo nozzle and the roll or work piece, said shield permitting a relatively high proportion of the spray to pass through the aperture in one configuration of spray envelope and a relatively low proportion of the spray to pass at another configuration of spray envelope, thereby to provide an additional degree of control over the outflow reaching the roll or work piece.
24. A rolling mill substantially as hereinbefore 0 described with reference to Figure 3 or Figures 4 and of the accompanying drawings. 00 DATED this 24th day of MARCH, 1992 i 0 s WILLIAM JOHN EDWARDS Attorney: LEON K. ALLEN Fellow Institute of Patent Attorneys of Australia of SHELSTON WATERS Nc 20 ABSTRACT The invention relates to a method for controlling the temperature of a work roll or work piece in a rolling mill, said method comprising the steps of: directing a first flow of a coolant or lubricant to a primary inlet (21) of a vortex valve directing a second flow of a coolant or lubricant having a characteristic substantially different from that of said first flow to a control I inlet (30) of the vortex valve; 000. mixing the first flow with the second flow within the vortex valve conducting a mixed outflow from an outlet (23) of the vortex valve to the work roll or work piece; and varying the flow rate of the second flow thereby to control the outflow conducted from the vortex valve to the roll or work piece in respect :of both flow rate and said characteristic. _0 ';ine (0)o tevoAeLale 0 c mxn tefis lo it h scndfo
AU18005/88A 1987-05-28 1988-05-24 Coolant flow control Ceased AU624575B2 (en)

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AUPI2206 1987-05-28
AUPI220687 1987-05-28
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4936127A (en) * 1989-05-25 1990-06-26 Asarco Incorporated Production of copper rod by rolling
CN113714299B (en) * 2021-08-30 2023-10-24 攀钢集团攀枝花钢钒有限公司 Rolling mill roller cooling method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1238804A (en) * 1968-06-06 1971-07-14
JPS54125162A (en) * 1978-03-23 1979-09-28 Sumitomo Metal Ind Ltd Controlling method for crown of skinpass roll
US4706480A (en) * 1985-10-11 1987-11-17 Svatos Joseph D Rolling mill cooling system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1238804A (en) * 1968-06-06 1971-07-14
JPS54125162A (en) * 1978-03-23 1979-09-28 Sumitomo Metal Ind Ltd Controlling method for crown of skinpass roll
US4706480A (en) * 1985-10-11 1987-11-17 Svatos Joseph D Rolling mill cooling system

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