US3241247A - Method of and apparatus for drying stereotype mats - Google Patents

Method of and apparatus for drying stereotype mats Download PDF

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US3241247A
US3241247A US100981A US10098161A US3241247A US 3241247 A US3241247 A US 3241247A US 100981 A US100981 A US 100981A US 10098161 A US10098161 A US 10098161A US 3241247 A US3241247 A US 3241247A
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mat
air
auxiliary
main
chamber
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US100981A
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Craig C Baker
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Sta-Hi Corp
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Sta-Hi Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41DAPPARATUS FOR THE MECHANICAL REPRODUCTION OF PRINTING SURFACES FOR STEREOTYPE PRINTING; SHAPING ELASTIC OR DEFORMABLE MATERIAL TO FORM PRINTING SURFACES
    • B41D1/00Preparing or treating stereotype matrices

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  • An important object of the present invention is to provide a method of and apparatus for pre-drying or forming mats wherein ⁇ air is circulated, i.e., caused to flow', adjacent both sides of the mat so as to remove moisture from both sides of the mat simultaneously.
  • the air circulated adjacent the supported side of the mat is preferably at subatmospheric pressure, while the air circula-ted adjacent the other side of the mat may be at atmospheric pressure, subatmospheric pressure, or superatmospheric pressure.
  • the pressure applied to the supported side of the mat is lower than the pressure applied to the other side thereof so as to produce across the mat a pressure ⁇ differential holding the mat against the foraininous member.
  • Controllingr the air pressure on and circulating air adjacent both sides of the mat have a number of important advantages.
  • Another advantage of applying subatrnospheric pressures to both sides of the mat is that any stresses in the mat are relieved.
  • a further advantage, particularly in a former embodying the invention, is that the diiferential pressure may be made high enough, eg., several inches of mercury, irrespective of whether the high pressure component of the differential pressure is subatmospheric or superatmospheric, to form the mat properly without the use of a forming blanket acting on the unsupported side thereof.
  • the elimination of any blanket leaves the unsupported side of the mat exposed for any operations thereon which may be desired, and also leaves the 11nsupported side of the mat exposed for more eflicient heating thereof and for more efficient removal of moisture therefrom.
  • a pulsating differential pressure achieved by pulsating either the low pressure component of the pressure differential, the high pressure component thereof, or both, may be used to facilitate mat shrinkage during drying while still retaining the mat in engagement with the supporting foraminous member.
  • a further object of the invention is to provide an apparatus capable of achieving the foregoing which includes a main chamber on and communicating with the supported side of the mat and an auxiliary chamber on and communicating with the opposite sid-e of the mat, main and auxiliary pumps, eg., blowers, or fans being connected to the main and auxiliary cham-bers, respectively, to produce the desired low and high pressure components in the main and auxiliary chambers, respectively, and to circulate air through the main and auxiliary chambers, respectively, so as to remove moisture from both sides of the mat simultaneously.
  • main and auxiliary pumps eg., blowers, or fans being connected to the main and auxiliary cham-bers, respectively, to produce the desired low and high pressure components in the main and auxiliary chambers, respectively, and to circulate air through the main and auxiliary chambers, respectively, so as to remove moisture from both sides of the mat simultaneously.
  • valve means for selectively connecting the inlet ⁇ and the outlet of each pump to the corresponding chamber and the atmosphere in such a manner as to produce any desired pressure, e.g., subatmospheric or superatmospheric, in the chamber, and in such a manner as to disi charge vall of the .air removed from the corresponding chamber to exhaust and introduce only atmospheric air thereint-o.
  • Another object is to recirculate part of the air removed from the corresponding chamber back into such chamber while discharging part of th-e removed air to exhaust and replacing it with atmospheric air.
  • a further object is to continuously recirculate all of the air removed from the corresponding chamber with no removed air being discharged to exhaust and with no removed air being added.
  • Another object is to remove moisture from any such recirculated air.
  • each of the auxiliary and main chambers may be operated on ⁇ a complete recirculation basis, on a partial recirculation basis, or on a nonrecirculating basis.
  • Another object ⁇ of the invention is to provide filter means in series with each pump and chamber for filtering the air introduced into the lcorresponding chamber, irrespective of Whether such air be atmospheric air, or recirculated air.
  • Another object is to provide in series with each pump and chamber heat exchanger means for transferring heat from the air removed from the chamber to the air introduced into the chamber, whether the introduced air be recirculated air, or atmospheric air.
  • an apparatus which includes radiant heating means in the main and auxiliary chambers for radiantly heating both ⁇ sides of the mat and/ or to provide heaters in ⁇ series with the respective pumps and chambers for heating the air introduced into the respective chambers.
  • radiant heating means in the main and auxiliary chambers for radiantly heating both ⁇ sides of the mat and/ or to provide heaters in ⁇ series with the respective pumps and chambers for heating the air introduced into the respective chambers.
  • both types of heating are utilized, the radiant heaters directly heating both sides of the mat and the heaters in series with the respective pumps and chambers serving to heat the air introduced into the respective chambers to increase its moisture carrying capacity.
  • FIG. 1 is a diagrammatic view of an apparatus which embodies the Iinvention and is capable of performing the method thereof;
  • FIG. 2 is a View similar to FIG. 1, but illustrating a different yset of operating conditions
  • FIG. 3 is a view similar to FIGS. 1 and 2, but illustrating still another set of operating conditions.
  • the numeral 10 designates Ia mat which is supported by and one side of which is in engagement with a foraminous member 12 forming one wall of a main air chamber 14, the foraminous member being a screen, a penforated plate, or the like.
  • the supported :side of the mat 10 is exposed to the pressure in the main chamber 14 through the foraminous member 12.
  • auxiliary air chamber 16 On the opposite, or unsupported, side of the mat 10 is an auxiliary air chamber 16, the unsupported side of the mat being exposed to the pressure in the auxiliary chamber.
  • the unsupported side of the mat 10 communicates with the auxiliary ⁇ chamber 16 through a second foraminous member 18 which forms one Wall of the auxiliary chamber.
  • the mat 10 normally does not engage the foraminous member 18.
  • any suitable construction may be provided to permit insertion of the mat between and removal thereof from between the main and auxiliary chambers 14 and 16.
  • the mat 10 may merely be inserted into and Withdrawn from the space between the ⁇ foraminous members 12 and 18.
  • one of the chambers 14 and 16 may be mounted for movement toward and away from the other, a suitable seal 26 being provided therebetween.
  • the mat 10 is shown in curved condition, as would be the case in a former, it may be in la flat condition, as would preferably be the case in a predryer. In the latter event, the foraminous members 12 and 18 would be at and the main and auxiliary chambers 14 and 16 would be complementarily shaped.
  • the supported and unsupported sides of the mat 10 are respectively heated by radiant heaters 22 and 24 respectively disposed in the main and auxiliary chambers 14 and 16.
  • Each of the heaters 22 and 24 may comprise a plurality of infrared lamps, preferably of the tube type. 1t is important to note that the supported and unsupported sides of the mat 10 are respectively directly exposed to the heaters 22 ⁇ and 2.4, through the respective oraminous members 12 and 18, for maximum heating efficiency.
  • the main and auxiliary chambers 14 and 16 have air inlet lines 26 and 28 respectively communicating therewith intermediate their ends or edges, and respectively have two outlet lines 30 and 32 communicating therewith at both ends or edges. With this construction, the air ow into each chamber 14 and 16 divides ⁇ and flows in both directions from .the middle of the chamber to insure uniform air circulation over the corresponding side of the mat 10.
  • the outlet lines 30 and 32 respectively lead to filters 34 and 36 which filter the air removed from the main and auxiliary chambers 14 and 16 so that it will be clean in the event that it is recirculated back to such chambers, as hereinafter discussed.
  • the ⁇ air removed from the main and auxiliary chambers 14 and 16 tlows through heat exchanger means or heat exchangers 38 and 40 which extract moisture from the air withdrawn from the chambers 14 and 16 by removing heat therefrom.
  • the air withdrawn from the main and auxiliary chambers 14 and 16 is dried by the respective heat exchangers 38 Iand 40 to increase its moisture absorbing capacity in the event of recirculation, or to reduce its humidifying etfect in the event it is discharged into .the air in a room.
  • Cool air is supplied to the heat exchangers 38 and 40, to cool the air withdrawn from the respective chambers 14 and 16, through lines 42 and 44, as will be described.
  • the line 42 is connected to the inlet line 26 leading to the main chamber 14 through the heat exchanger 38 and a heater ⁇ 46.
  • valves 5t have ports 54 and 56 respectively connected to the heat exchangers 38 and 40, ports 58 and 68 respectively communicating with the atmosphere, ports 62 and 64 respectively communicating with filters 66 and 68 which respectively communicate in turn With the atmosphere at 70 and 72, and ports 74 and 76 respectively connected to the inlets of main ⁇ and auxiliary pumps 78 and 80, which may be centrifugal blowers, for example.
  • various ow patterns may be produced by selecting different positions for the valves 56 and 52.
  • the apparatus of the invention also includes four-way valves 82 and 84 which cooperate with the four-way valves 50 and 52, respectively, as will be described.
  • the valves 82 and 84 are respectively provided with ports 86 and 88 communicating with the outlets of the main and auxiliary pumps 78 and 80, ports 90 and 92 communicating with the atmosphere, ports 94 and 96 connected to the lines 42 and 44 leading to the heat exchangers 38 and 40, and ports 98 and 100 leading to the filter 66 and to a filter 102, the latter communicating with the atmosphere at 104.
  • the mat 10 may be held against the foraminous member 12 by a pressure differential between the main and auxiliary chambers 14 and 16 at least the low pressure component of which, i.e., the pressure in the main chamber 14, is subatmospheric (although this is not absolutely essential).
  • T-he high pressure component of the pressure differential i.e., the pressure in the auxiliary chamber 16 may be any value, subatmospheric, atmospheric, or superatmospheric, higher than the pressure in the main chamber 14.
  • the pressures in both the main and auxiliary chambers 14 and 16 are subatmospheric to expedite drying of the mat 10 as hereinbefore explained.
  • valves 50 and 82 are in positions such that all of the air withdrawn from the main chamber 14 is discharged to exhaust at 98 through the main pump 78.
  • the air introduced into the main chamber 14 and flowing over the supported side of the mat 10 is all fresh atmospheric air passing through the filter 66, the valve 82, the heat exchanger 38 and the heater 46, and bypassing the main pump 7 8. Consequently, a subatmospheric pressure is produced in the main chamber 14.
  • valves 52 and 84 are so positioned that all of the air removed from the auxiliary chamber 16 is discharged to exhaust at 60, and all of the air entering the auxiliary chamber and flowing over the unsupported side of the mat 10 is fresh atmospheric air owing through the filter 68, the valve 52, the auxiliary pump 88, the valve 84, the heat exchanger 40 and the heater 48. It will be noted that the air withdrawn from the auxiliary chamber 16 bypasses the auxiliary pump 80, with the result the pressure in the auxiliary chamber 16 is superatmospheric.
  • the pressure differential acting on the mat 10 is the ⁇ difference between the subatmospheric pressure in the main chamber 14 and the superatmospheric pressure in the auxiliary chamber 16. This pressure differential may have any desired magnitude, ranging from zero to a maximum depending on the sum of the capacities of the main and auxiliary pumps 78 and 80.
  • the heat exchangers 38 and 441 pre-heat the air introduced into the main and auxiliary chambers 14 and 16, extracting heat from the air withdrawn from such chambers.
  • the heat exchangers 38 and 40 also extract moisture from the air withdrawn from the chambers 14 and 16, which is advantageous in the event that the Withdrawn air is discharged into a room, although it may be discharged out of doors, as will be understood.
  • the positions of the valves 50 and 82 are the same as showin in FIG. 1, whereby subatmospheric pressure obtains in the main chamber 14.
  • the positions of the valves 52 and 84 are such that all of the air withdrawn from the auxiliary chamber 16 is discharged to exhaust at 92 through the auxiliary pump 80, and fresh atmospheric air is introduced into the auxiliary chamber 16 through the -lter 102, the valve yS4, the heat exchanger 40 and the heater 48 so that the auxiliary pump 80 is bypassed. Consequently, subatrnospheric pressure exists in the auxiliary chamber 16 also.
  • the pressure on the mat can be varied from zero to the maximum subatmospheric pressure attainable in either the main chamber 14 or the auxiliary chamber 16, whereas with the conditions of FIG. 1, the pressure on the mat can be varied between zero and the sum of the maximum subatmospheric and superatrnospheric pressures attainable in the chambers 14 and 16.
  • a pulsating diiferential pressure, rst biasing the mat 10 toward the foraminous member 12 and then biasing it away from this foraminous member can be applied to promote shrinkage.
  • This effect may be produced by suitable manual or automatic manipulations of appropriate ones of the valves 50, 52, 82 and 84.
  • the exhaust air is cool and dry under the conditions of FIG. 2.
  • valves 82 yand $4 are so positioned that part of the air withdrawn from the chambers 14 and 16 through the main and auxiliary pumps '7S and 80 is directed back to these chambers by the valves mentioned, the remainder being discharged to exhaust at 90 and 92.
  • no ⁇ air from the atmosphere is being introduced into the main and auxiliary chambers 14 and 16 (except through leakage) so that the maximum subatmospheric pressures of which the main and auxiliary pumps 7 8 and 80 are capable are produced in these chambers.
  • the capacity of the main pump 78 exceeds that of the auxiliary pump 80 so that when the maximum vacuums of which the main and auxiliary pumps are capable are produced in the main and auxiliary chambers 14 and 16, the pressure in the main chamber is lower than that in the auxiliary chamber so that a pressure didereutial exists tending to hold the mat 10 against the foraminous member 12.
  • FIG. 3 of the drawings can be modied, if desired, by so positioning the valves 50 and 52 that some atmospheric air is drawn into the inlets of the main and auxiliary pumps 78 and 80 through the filters 66 and 68, respectively, by way of the ports 62 and 64. This limits the vacuums which can be achieved in the main and auxiliary chambers 14 and 16 should this be desired.
  • valves Si), 52, 82 and 84 may be used to obtain pressure relations in the main and auxiliary chambers 14 and 16, and corresponding flow patterns, which are not shown in the drawings.
  • auxiliary control equipment may be used in conjunction with the apparatus hereinhefore disclosed.
  • means may be provided for measuring the moisture content of the air in, or leaving, the main and auxiliary chambers 14 and 16 and for terminating operation of the apparatus when the moisture content has been reduced to a desired level.
  • means may be provided for terminating the cycle in response to shrinkage of the mat 10.
  • a method of drying a mat characterized by the use of a foraminous wall engageable by one side of the mat, and including the steps of:
  • said pumping means including a main pump connected to said main chamber and an auxiliary pump connected to said auxiliary chamber;
  • said pumping means including a main exhaust pump having an inlet connected to said main chamber and an auxiliary exhaust pump having an inlet connected to said auxiliary chamber;
  • said pumping means including a main pump connected to said main chamber and an auxiliary pump connected to said auxiliary chamber;
  • each of said main and auxiliary pumps having an inlet and an outlet;
  • valve means for selectively connecting said inlet and said outlet of said main pump to said main chamber and the atmosphere;
  • valve means for selectively connecting said inlet and said outlet of said auxiliary pump to said auxiliary chamber and the atmosphere;
  • An apparatus according to claim 6 including:
  • heating means includes:
  • heating means includes radiant heaters in said main and auxiliary chambers

Description

March 22, 196s C, c. BAKER 3,241,247
METHOD OF AND APPARATUS FOR DRYING STEREOTYPE MATS Filed April 5. 1961 5 Sheets-Sheet 1 INVENTOR.
,Hiep/q ,l/Eng, .Has-ELL @JL/ERM March`22, 1966 C. c, BAKER 3,241,247
METHOD OF AND APPARATUS FOR DRYING STEREOTYPE MATS Filed April s, 1961 5 Sheets-Sheet 2 2M/9 l gmfel?,
INVENTOR.
BY '/fs Arran/Veys.
Hike/s, ,lf/saw, Hassan, lien/vf March 22, 1966 c. c. BAKER 3,241,247
METHOD OF AND APPARATUS FOR DRYING STEREOTYPE MATS Filed April 5. 1961 5 Sheets-Sheet 5 r/.nm/'g/ Chamber .l Gram/Says Maf@ Member J2 Ham/n0g; 52 Member- .fi
L {L` 224/5 C1 BAA/EQ,
Z? INVENTOR.
BY //S rraR/VE ST .Hime/s, .37E-Chg i?asssLL may United States Patent O 3,241,247 METHOD F AND APPARATUS FOR DRYING STEREOTYPE MATS Craig C. Baker, Arcadia, Calif., assignor to Sta-Hi Corporation, Whittier, Calif., a corporation of California Filed Apr. 5, 1961, Ser. No. 100,981 Claims. (Cl. 34-17) The present invention relates in general to drying materials in sheet form and since it finds particular utility in the eld of drying stereotype mats it will be considered in such connection herein for convenience of disclosure.
In general, it is an object of the present invention to provide an improved method of and apparatus for drying and shrinking stereotype mats, either in so-called pre dryer, or in a former wherein the iinal forming, drying and shrinking operations prior to casting are performed on the mats.
It is conventional in pre-drying or forming stereotype mats to support one side of the mat on a foraminous member, such as a screen, a perforated plate, or the like, and to apply a vacuum to the supported side of the mat to hold it against the forarnirious member. A-t the same time, the mat is heated to drive on excess moisture. With this construction, moisture is removed from the mat on one side thereof only, i.e., on the side thereof which is supported by the foraminous member.
An important object of the present invention is to provide a method of and apparatus for pre-drying or forming mats wherein `air is circulated, i.e., caused to flow', adjacent both sides of the mat so as to remove moisture from both sides of the mat simultaneously. The air circulated adjacent the supported side of the mat is preferably at subatmospheric pressure, while the air circula-ted adjacent the other side of the mat may be at atmospheric pressure, subatmospheric pressure, or superatmospheric pressure. In any event, the pressure applied to the supported side of the mat is lower than the pressure applied to the other side thereof so as to produce across the mat a pressure `differential holding the mat against the foraininous member.
Controllingr the air pressure on and circulating air adjacent both sides of the mat, as opposed to the conventional practice of merely applying a vacuum to the supported side thereof, have a number of important advantages. First, by using subatmospheric pressures on both sides of the mat, it is possible to signicantly reduce the temperature at which the moisture in the mat will evaporate, thereby permitting a .reduction in the time required to reduce the `moisture content to the desired level and/or the heat required to accomplish this. Another advantage of applying subatrnospheric pressures to both sides of the mat is that any stresses in the mat are relieved. A further advantage, particularly in a former embodying the invention, is that the diiferential pressure may be made high enough, eg., several inches of mercury, irrespective of whether the high pressure component of the differential pressure is subatmospheric or superatmospheric, to form the mat properly without the use of a forming blanket acting on the unsupported side thereof. The elimination of any blanket leaves the unsupported side of the mat exposed for any operations thereon which may be desired, and also leaves the 11nsupported side of the mat exposed for more eflicient heating thereof and for more efficient removal of moisture therefrom. It will be understood that a pulsating differential pressure, achieved by pulsating either the low pressure component of the pressure differential, the high pressure component thereof, or both, may be used to facilitate mat shrinkage during drying while still retaining the mat in engagement with the supporting foraminous member.
Mice
A further object of the invention is to provide an apparatus capable of achieving the foregoing which includes a main chamber on and communicating with the supported side of the mat and an auxiliary chamber on and communicating with the opposite sid-e of the mat, main and auxiliary pumps, eg., blowers, or fans being connected to the main and auxiliary cham-bers, respectively, to produce the desired low and high pressure components in the main and auxiliary chambers, respectively, and to circulate air through the main and auxiliary chambers, respectively, so as to remove moisture from both sides of the mat simultaneously.
Other and important objects of the invention are to provide valve means for selectively connecting the inlet `and the outlet of each pump to the corresponding chamber and the atmosphere in such a manner as to produce any desired pressure, e.g., subatmospheric or superatmospheric, in the chamber, and in such a manner as to disi charge vall of the .air removed from the corresponding chamber to exhaust and introduce only atmospheric air thereint-o. Another object is to recirculate part of the air removed from the corresponding chamber back into such chamber while discharging part of th-e removed air to exhaust and replacing it with atmospheric air. A further object is to continuously recirculate all of the air removed from the corresponding chamber with no removed air being discharged to exhaust and with no removed air being added. Another object is to remove moisture from any such recirculated air. With such constructions, each of the auxiliary and main chambers may be operated on `a complete recirculation basis, on a partial recirculation basis, or on a nonrecirculating basis.
Another object `of the invention is to provide filter means in series with each pump and chamber for filtering the air introduced into the lcorresponding chamber, irrespective of Whether such air be atmospheric air, or recirculated air.
Another object is to provide in series with each pump and chamber heat exchanger means for transferring heat from the air removed from the chamber to the air introduced into the chamber, whether the introduced air be recirculated air, or atmospheric air. The heat exchanger means in `series with each pump and chamber, `in addition to pre-heating the air introduced into such chamber, also has the effect of cooling the air removed from such chamber so as to reduce its moisture content, which is an important feature.
Other objects are to provide an apparatus which includes radiant heating means in the main and auxiliary chambers for radiantly heating both `sides of the mat and/ or to provide heaters in `series with the respective pumps and chambers for heating the air introduced into the respective chambers. Preferably, both types of heating are utilized, the radiant heaters directly heating both sides of the mat and the heaters in series with the respective pumps and chambers serving to heat the air introduced into the respective chambers to increase its moisture carrying capacity.
The foregoing objects, advantages, features and results of the present invention, together with various other objects, advantages, features and results thereof which will be evident to those `skilled in the art to which the invention relates in the light of this disclosure, may be achieved with the exemplary embodiment of the invention described in detail hereinafter and illustrated in the accompanying drawings, in which:
FIG. 1 is a diagrammatic view of an apparatus which embodies the Iinvention and is capable of performing the method thereof;
FIG. 2 is a View similar to FIG. 1, but illustrating a different yset of operating conditions; and
FIG. 3 is a view similar to FIGS. 1 and 2, but illustrating still another set of operating conditions.
In each of FIGS. 1 to 3 of the drawings, the numeral 10 designates Ia mat which is supported by and one side of which is in engagement with a foraminous member 12 forming one wall of a main air chamber 14, the foraminous member being a screen, a penforated plate, or the like. As will be apparent, the supported :side of the mat 10 is exposed to the pressure in the main chamber 14 through the foraminous member 12.
On the opposite, or unsupported, side of the mat 10 is an auxiliary air chamber 16, the unsupported side of the mat being exposed to the pressure in the auxiliary chamber. In the particular construction illustrated, the unsupported side of the mat 10 communicates with the auxiliary `chamber 16 through a second foraminous member 18 which forms one Wall of the auxiliary chamber. However, the mat 10 normally does not engage the foraminous member 18.
Any suitable construction may be provided to permit insertion of the mat between and removal thereof from between the main and auxiliary chambers 14 and 16. For example, the mat 10 may merely be inserted into and Withdrawn from the space between the ` foraminous members 12 and 18. Alternatively, one of the chambers 14 and 16 may be mounted for movement toward and away from the other, a suitable seal 26 being provided therebetween. Also, while the mat 10 is shown in curved condition, as would be the case in a former, it may be in la flat condition, as would preferably be the case in a predryer. In the latter event, the foraminous members 12 and 18 would be at and the main and auxiliary chambers 14 and 16 would be complementarily shaped.
The supported and unsupported sides of the mat 10 are respectively heated by radiant heaters 22 and 24 respectively disposed in the main and auxiliary chambers 14 and 16. Each of the heaters 22 and 24 may comprise a plurality of infrared lamps, preferably of the tube type. 1t is important to note that the supported and unsupported sides of the mat 10 are respectively directly exposed to the heaters 22 `and 2.4, through the respective oraminous members 12 and 18, for maximum heating efficiency.
The main and auxiliary chambers 14 and 16 have air inlet lines 26 and 28 respectively communicating therewith intermediate their ends or edges, and respectively have two outlet lines 30 and 32 communicating therewith at both ends or edges. With this construction, the air ow into each chamber 14 and 16 divides `and flows in both directions from .the middle of the chamber to insure uniform air circulation over the corresponding side of the mat 10.
The outlet lines 30 and 32 respectively lead to filters 34 and 36 which filter the air removed from the main and auxiliary chambers 14 and 16 so that it will be clean in the event that it is recirculated back to such chambers, as hereinafter discussed.
From the lters 34 and 36, the `air removed from the main and auxiliary chambers 14 and 16 tlows through heat exchanger means or heat exchangers 38 and 40 which extract moisture from the air withdrawn from the chambers 14 and 16 by removing heat therefrom. Thus, the air withdrawn from the main and auxiliary chambers 14 and 16 is dried by the respective heat exchangers 38 Iand 40 to increase its moisture absorbing capacity in the event of recirculation, or to reduce its humidifying etfect in the event it is discharged into .the air in a room.
Cool air is supplied to the heat exchangers 38 and 40, to cool the air withdrawn from the respective chambers 14 and 16, through lines 42 and 44, as will be described. The line 42 is connected to the inlet line 26 leading to the main chamber 14 through the heat exchanger 38 and a heater `46. Similarly, air flows from the line 44 through the heat exchanger 40, a heater 48, and the inlet line 23 yinto the auxiliary chamber 16.
The iltered `and cooled, and thus dried, air removed from the main and auxiliary chambers 14 and 16, after passing through the heat exchangers 38 and 40, ows to four- way valves 50 and 52, respectively. More particcularly, the valves 5t have ports 54 and 56 respectively connected to the heat exchangers 38 and 40, ports 58 and 68 respectively communicating with the atmosphere, ports 62 and 64 respectively communicating with filters 66 and 68 which respectively communicate in turn With the atmosphere at 70 and 72, and ports 74 and 76 respectively connected to the inlets of main `and auxiliary pumps 78 and 80, which may be centrifugal blowers, for example. As will be discussed .in more detail hereinafter, various ow patterns may be produced by selecting different positions for the valves 56 and 52.
The apparatus of the invention also includes four- way valves 82 and 84 which cooperate with the four- way valves 50 and 52, respectively, as will be described. The valves 82 and 84 are respectively provided with ports 86 and 88 communicating with the outlets of the main and auxiliary pumps 78 and 80, ports 90 and 92 communicating with the atmosphere, ports 94 and 96 connected to the lines 42 and 44 leading to the heat exchangers 38 and 40, and ports 98 and 100 leading to the filter 66 and to a filter 102, the latter communicating with the atmosphere at 104.
The foregoing completes a description of the structure of the apparatus of the invention which is shown in the drawings, and its various modes of operation will now be considered.
Operation As hereinbefore suggested, the mat 10 may be held against the foraminous member 12 by a pressure differential between the main and auxiliary chambers 14 and 16 at least the low pressure component of which, i.e., the pressure in the main chamber 14, is subatmospheric (although this is not absolutely essential). T-he high pressure component of the pressure differential, i.e., the pressure in the auxiliary chamber 16, may be any value, subatmospheric, atmospheric, or superatmospheric, higher than the pressure in the main chamber 14. Preferably, the pressures in both the main and auxiliary chambers 14 and 16 are subatmospheric to expedite drying of the mat 10 as hereinbefore explained.
The foregoing various pressure component patterns, and corresponding fiow patterns through the apparatus, are achieved by means of the four- way valves 50, 52, 82 and 84. Various pressure and ow patterns will now be considered in connection with the respective figures of the drawings.
Considering first the conditions obtaining in FIG. 1 of the drawings, the valves 50 and 82 are in positions such that all of the air withdrawn from the main chamber 14 is discharged to exhaust at 98 through the main pump 78. The air introduced into the main chamber 14 and flowing over the supported side of the mat 10 is all fresh atmospheric air passing through the filter 66, the valve 82, the heat exchanger 38 and the heater 46, and bypassing the main pump 7 8. Consequently, a subatmospheric pressure is produced in the main chamber 14.
Similarly, the valves 52 and 84 are so positioned that all of the air removed from the auxiliary chamber 16 is discharged to exhaust at 60, and all of the air entering the auxiliary chamber and flowing over the unsupported side of the mat 10 is fresh atmospheric air owing through the filter 68, the valve 52, the auxiliary pump 88, the valve 84, the heat exchanger 40 and the heater 48. It will be noted that the air withdrawn from the auxiliary chamber 16 bypasses the auxiliary pump 80, with the result the the pressure in the auxiliary chamber 16 is superatmospheric. The pressure differential acting on the mat 10 is the `difference between the subatmospheric pressure in the main chamber 14 and the superatmospheric pressure in the auxiliary chamber 16. This pressure differential may have any desired magnitude, ranging from zero to a maximum depending on the sum of the capacities of the main and auxiliary pumps 78 and 80.
It will be noted that, with the conditions obtaining in FIG. l, the heat exchangers 38 and 441 pre-heat the air introduced into the main and auxiliary chambers 14 and 16, extracting heat from the air withdrawn from such chambers. The heat exchangers 38 and 40 also extract moisture from the air withdrawn from the chambers 14 and 16, which is advantageous in the event that the Withdrawn air is discharged into a room, although it may be discharged out of doors, as will be understood.
Referring to FIG. 2 of the drawings, the positions of the valves 50 and 82 are the same as showin in FIG. 1, whereby subatmospheric pressure obtains in the main chamber 14. However, the positions of the valves 52 and 84 are such that all of the air withdrawn from the auxiliary chamber 16 is discharged to exhaust at 92 through the auxiliary pump 80, and fresh atmospheric air is introduced into the auxiliary chamber 16 through the -lter 102, the valve yS4, the heat exchanger 40 and the heater 48 so that the auxiliary pump 80 is bypassed. Consequently, subatrnospheric pressure exists in the auxiliary chamber 16 also. Under such conditions, the pressure on the mat can be varied from zero to the maximum subatmospheric pressure attainable in either the main chamber 14 or the auxiliary chamber 16, whereas with the conditions of FIG. 1, the pressure on the mat can be varied between zero and the sum of the maximum subatmospheric and superatrnospheric pressures attainable in the chambers 14 and 16. With the conditions of FIG. 2, a pulsating diiferential pressure, rst biasing the mat 10 toward the foraminous member 12 and then biasing it away from this foraminous member, can be applied to promote shrinkage. This effect may be produced by suitable manual or automatic manipulations of appropriate ones of the valves 50, 52, 82 and 84. As is the case with the conditions of FIG. l, the exhaust air is cool and dry under the conditions of FIG. 2.
Referring to FIG. 3 of the drawings, the conditions shown therein are the same as those shown in FIG. 2, except that the valves 82 yand $4 are so positioned that part of the air withdrawn from the chambers 14 and 16 through the main and auxiliary pumps '7S and 80 is directed back to these chambers by the valves mentioned, the remainder being discharged to exhaust at 90 and 92. Under these conditions, no `air from the atmosphere is being introduced into the main and auxiliary chambers 14 and 16 (except through leakage) so that the maximum subatmospheric pressures of which the main and auxiliary pumps 7 8 and 80 are capable are produced in these chambers. The capacity of the main pump 78 exceeds that of the auxiliary pump 80 so that when the maximum vacuums of which the main and auxiliary pumps are capable are produced in the main and auxiliary chambers 14 and 16, the pressure in the main chamber is lower than that in the auxiliary chamber so that a pressure didereutial exists tending to hold the mat 10 against the foraminous member 12.
The conditions existing in FIG. 3 of the drawings can be modied, if desired, by so positioning the valves 50 and 52 that some atmospheric air is drawn into the inlets of the main and auxiliary pumps 78 and 80 through the filters 66 and 68, respectively, by way of the ports 62 and 64. This limits the vacuums which can be achieved in the main and auxiliary chambers 14 and 16 should this be desired.
Various other relative settings of the valves Si), 52, 82 and 84 may be used to obtain pressure relations in the main and auxiliary chambers 14 and 16, and corresponding flow patterns, which are not shown in the drawings.
It will be understood that various auxiliary control equipment may be used in conjunction with the apparatus hereinhefore disclosed. For example, means may be provided for measuring the moisture content of the air in, or leaving, the main and auxiliary chambers 14 and 16 and for terminating operation of the apparatus when the moisture content has been reduced to a desired level. Alternatively, or in addition, means may be provided for terminating the cycle in response to shrinkage of the mat 10.
Although an exemplary embodiment of the invention has been disclosed for purposes of illustration, it will be understood that various changes, modifications and substitutions may be incorporated therein without departing from the spirit of the invention as dened. by the claims which follow.
I claim:
1. A method of drying a mat, characterized by the use of a foraminous wall engageable by one side of the mat, and including the steps of:
(a) placing said one side of the mat adjacent said foraminous Wall;
(b) flowing a irst stream of air past said foraminous Wall so as to remove moisture exaporated from said one side of the mat;
(c) owing a second, separate stream of air past the other side of the mat so as to separately remove moisture exaporated from said other side of the mat;
(d) maintaining the pressure in said iirst stream below the pressure in said second stream so as to create between said streams an air pressure differential acting in a directionrto urge said one side of the mat into engagement with said foraminous wall; and
(e) heating both sides of said mat to evaporate moisture therefrom into the respective, separate streams of air so that the moisture evaporated from said one side of said mat is carried away independently of the moisture evaporated from said other side of said mat.
2. In .an apparatus for drying a mat, the combination (a) a foraminous member adapted to support a mat on one side thereof;
(b) means providing a main air chamber on the other side of and communicating with said foraminous member;
(c) means providing an auxiliary air chamber on said one side of and communicating with said foraminous member;
(d) means for flowing separate, main and auxiliary streams of air through said main and auxiliary chambers, respectively, so as to separately remove moisture evaporated from opposite sides of a mat supported by said foraminous member, and for simulaneously maintaining the pressure in said main air chamber below the pressure in said auxiliary air chamber so as to create an air pressure differential acting to hold the mat against said one side of said foraminous member; and
(e) means for radiantly heating both sides of a mat held against said one side of said foraminous member by said air pressure differential.
3. In an apparatus for drying a mat, the combination (a) a foraminous member adapted to support a mat on one side thereof;
(b) means providing a main air chamber on the other side of and communicating with said foraminous member;
(c) means providing an auxiliary air chamber on said one side of and communicating with said foraminous member;
(d) pumping means for flowing separate, main and auxiliary streams of air through said main and auxiliary chambers, respectively, so as to separately remove moisture evaporated from opposite sides of a mat supported by said foraminous member, and
for simultaneously maintaining the pressure in said main air chamber below the pressure in said auxiliary air chamber so as to create an air pressure differential acting to hold the mat against said one side of said foraminous member;
(e) said pumping means including a main pump connected to said main chamber and an auxiliary pump connected to said auxiliary chamber; and
(f) means for radiantly heating both sides of a mat held against said one side of said foraminous member by said air pressure differential.
4. In an apparatus for drying a mat, the combination of:
(a) a foraminous member adapted to support a mat on one side thereof;
(b) means providing a main air chamber on the other side of and communicating with said foraminous member and having an inlet communicating with the atmosphere;
(c) means providing an auxiliary air chamber on said one side `of and communicating with said foraminous member and having an inlet communicating with the atmosphere;
(d) pumping means for flowing separate, main and auxiliary streams of air through said main and auxiliary chambers, respectively, from their respective inlets so as to separately remove moisture evaporated from opposite sides of a mat supported by said foraminous member, and for simultaneously maintaining the pressure in said main air chamber below the pressure in said auxiliary air chamber so as to create an air pressure diierential acting to hold the mat against said one side of said foraminous member;
(e) said pumping means including a main exhaust pump having an inlet connected to said main chamber and an auxiliary exhaust pump having an inlet connected to said auxiliary chamber; and
(f) means for radiantly heating both sides of a mat held against said one side of said foraminous member by said air pressure differential.
5. In an apparatus for drying a mat, the combination of:
(a) a curved foraminous member having concave and convex sides and adapted to support a mat on said convex side thereof;
(b) means providing a main air chamber on the said concave side of and communicating with said foraminous member;
(c) means providing an auxiliary air chamber on said convex side of and communicating with said O- raminous member;
(d) means for owing separate, main and auxiliary streams of air through said main and auxiliary chambers, respectively, so as to separately remove moisture evaporated from opposite sides of a mat supported by said foraminous member, and for simultaneously maintaining the pressure in said main air chamber below the pressure in said auxiliary air chamber so as to create an air pressure differential acting to hold the mat against said convex side of said foraminous member; and
(e) means for radiantly heating both sides of a mat held against said convex side of said foraminous member by said air pressure differential.
6. In an apparatus for drying a mat, the combination of:
(a) a foraminous member adapted to support a mat on one side thereof;
(b) means providing a main chamber on the other side of and communicating with said foraminous member;
(c) means providing an auxiliary chamber on said one side of and communicating with said foraminous member;
(d) pumping means for maintaining a pressure difierential, having high and low pressure components, between said auxiliary and main chambers with said high pressure component in said auxiliary chamber and said low pressure component in said main chamber, whereby to hold a mat against said one side of said foraminous member, and for simultaneously ilowing separate `streams of air through said auxiliary and main chambers;
(e) said pumping means including a main pump connected to said main chamber and an auxiliary pump connected to said auxiliary chamber;
(f) each of said main and auxiliary pumps having an inlet and an outlet;
(g) valve means for selectively connecting said inlet and said outlet of said main pump to said main chamber and the atmosphere;
(h) valve means for selectively connecting said inlet and said outlet of said auxiliary pump to said auxiliary chamber and the atmosphere; and
(i) means for heating both sides of a mat supported by said one side of said foraminous member 7. An apparatus as dened in claim 6 including:
(a) filter means for filtering air removed from and introduced into said main chamber; and
(b) filter means for filtering air removed from and introduced into said auxiliary chamber.
3. An apparatus according to claim 6 including:
(a) heat exchanger means for exchanging heat between air removed from and air introduced into said main chamber; and
(b) heat exchanger means for exchanging heat between air removed from and air introduced into said auxiliary chamber.
9. An apparatus according to claim 6 wherein said heating means includes:
(a) a heater in series with said main chamber for heating air introduced into said main chamber; and (b) a heater in series with said auxiliary chamber for heating air introduced into said auxiliary chamber.
lill. An apparatus according to claim 6 wherein said heating means includes radiant heaters in said main and auxiliary chambers,
References Cited bythe Examiner UNITED STATES PATENTS 1,960,697 5/1934 Cochran 34-146 2,095,118 10/1937 Basler 34 145 2,122,800 7/1938 Lougee .34*92 2,661,543 l2/1953 Tyndall 34--16 2,83 8,42() 6/1958 Valente 34-23 2,903,799 9/1959 Sachaczenski 34-82 FOREIGN PATENTS 199,669 3/1958 Austria.
WILLIAM F. ODEA, Primary Examiner. BENJAMIN BENDETT, Examiner'.
CHARLES OCONNELL, GEORGE D. MITCHELL,
NORMAN YUDKOFF, Assistant Examiners.
UNITED STATES PATENT OFFICE CERTIFICATE 0F CCRRECTION Patent Noh 3,241,247 March z2, 1966 Craig C. Baker It is hereby certified that error appears in the above numbered patent requiring correction and that the said Letters Patent should read as corrected below.
Column 6, lines 20 and 24, for "exaporated", each occurrence, read evaporated line S3, for "smulaneously read simultaneously Signed and sealed this 21st day of June l966 (SEAL) Attest:
ERNEST W. SWIDER EDWARD J. BRENNER Attesting Officer Commissioner of Patents

Claims (1)

  1. 2. IN AN APPARATUS FOR DRYING A MAT, THE COMBINATION OF: (A) A FORAMINOUS MEMBER ADAPTED TO SUPPORT A MAT ON ONE SIDE THEREOFF; (B) MEANS PROVIDING A MAIN AIR CHAMBER ON THE OTHER SIDE OF AND COMMUNICATING WITH SAID FORMAINOUS MEMBER; (C) MEANS PROVIDING AN AUXILIARY AIR CHAMBER ON SAID ONE SIDE OF AND COMMUNICATING WITH SAID FORAMINOUS MEMBER; (D) MEANS FOR FLOWING SEPARATE, MAIN AND AUXILIARY STREAMS OF AIR THROUGH SAID MAIN AND AUXILIARY CHAMBERS, RESPECTIVELY, SO AS TO SEPARATELY REMOVE MOISTURE EVAPORATED FROM OPPOSITE SIDES OF A MAT SUPPORTED BY SAID FORAMINOUS MEMBER, AND FOR SIMULTANEOUSLY MAINTAINING THE PRESSURE IN SAID MAIN AIR CHAMBER BELOW THE PRESSURE IN SAID AUXILIARY AIR CHAMBER SO AS TO CREATE AN AIR PRESSURE DIFFERENTIAL ACTING TO HOLD THE MAT AGAINST SAID ONE SIDE OF SAID FORAMINOUS MEMBER; AND
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3987556A (en) * 1972-04-26 1976-10-26 Olivier Tissot Apparatus for drying hides and skins

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1960697A (en) * 1931-02-02 1934-05-29 Albert W Cochran Improved matrix former and drier
US2095118A (en) * 1934-08-25 1937-10-05 Basler Hermann Device for the manufacture of plates, sheets, or slabs of various properties from vegetable fibrous pulp
US2122800A (en) * 1934-12-22 1938-07-05 Hoe & Co R Matrix drying machine
US2661543A (en) * 1950-06-24 1953-12-08 United Shoe Machinery Corp Apparatus for and methods of drying leather
US2838420A (en) * 1956-08-23 1958-06-10 Kimberly Clark Co Method for drying impregnated porous webs
AT199669B (en) * 1956-03-15 1958-09-25 Winkler Fallert & Co Maschf Device for drying stereotype matrices
US2903799A (en) * 1955-06-21 1959-09-15 Philco Corp Drying apparatus

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1960697A (en) * 1931-02-02 1934-05-29 Albert W Cochran Improved matrix former and drier
US2095118A (en) * 1934-08-25 1937-10-05 Basler Hermann Device for the manufacture of plates, sheets, or slabs of various properties from vegetable fibrous pulp
US2122800A (en) * 1934-12-22 1938-07-05 Hoe & Co R Matrix drying machine
US2661543A (en) * 1950-06-24 1953-12-08 United Shoe Machinery Corp Apparatus for and methods of drying leather
US2903799A (en) * 1955-06-21 1959-09-15 Philco Corp Drying apparatus
AT199669B (en) * 1956-03-15 1958-09-25 Winkler Fallert & Co Maschf Device for drying stereotype matrices
US2838420A (en) * 1956-08-23 1958-06-10 Kimberly Clark Co Method for drying impregnated porous webs

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3987556A (en) * 1972-04-26 1976-10-26 Olivier Tissot Apparatus for drying hides and skins

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