Process for producing a plastic sheet having parallel ribs extruding from both surfaces

Claim 2

A process for producing an unstretched bilaterally corrugated plastic sheet having a plurality of longitudinally extending parallel ribs on both sides thereof comprising extruding in a horizontal plane a plastic synthetic resin composition from a slotted nozzle which is fashioned to be comb-like on both sides thereof to form an extruded sheet having longitudinally extending parallel ribs on both sides thereof heated to an extrusion temperature, drawing off the extruded heated sheet in the longitudinal direction of the ribs from said slotted nozzle by conducting the sheet through a cooled smoothing calender, and cooling the extruded sheet within said calender to a temperature below the extrusion temperature to thereby form said unstretched bilaterally corrugated plastic sheet, said extruded sheet being drawn off from said nozzle at a fixed rate which is the same as or slightly more than the extrusion rate from said nozzle so that the ribs on said unstretched bilaterally corrugated plastic sheet exiting from said smoothing calender are uniform in size and shape, the height and width of the ribs being from about 1/15 to about equal to the thickness of a basic, non-ribbed, portion of the sheet and the basic, non-ribbed, portion of the sheet having a thickness of about 0.5 to 3 mm.

Claim 3

The process according to claim 1, wherein the arrangement of said cooled smoothing calender with respect to said slotted nozzle and the extent of cooling provided by said cooled smoothing calender are so selected that said extruded sheet solidifies as it passes through said calender.

Claim 4

The process according to claim 2, wherein the shape of said nozzle and the extent of the smoothing provided by said cooled smoothing calender are so selected that the ribs on the bilaterally corrugated plastic sheets are rectangular in cross-section.

Claim 5

The process according to claim 3, wherein said slotted nozzle exhibits a uniform mirror-symmetrical rib design so that the rib configuration on one side of the sheet is a substantially uniform, mirror-symmetrical image of the rib configuration on the other side of the sheet.

Claim 6

The process according to claim 1, wherein said plastic synthetic resin is soft PVC.

Claim 7

The process according to claim 1, wherein the plastic synthetic resin composition is extruded and drawn off in such a way that the height of said ribs exceeds about 0.2 mm.

Claim 8

The process of claim 6, wherein said plastic synthetic resin composition is extruded and drawn off in such a way that the spacing between the ribs is slightly larger than the width of said ribs.

Claim 9

The process according to claim 1, wherein said cooled smoothing calender comprises at least two parallel cylindrical rolls, said extruded sheet being passed between the nip between said rolls.

Claim 10

The process according to claim 8, wherein said extruded sheet tangentially engages one of said rolls prior to passage through said nip and further tangentially engages another of said rolls after passing through said nip.

Claim 11

The process according to claim 9, wherein said extruded sheet remains in contact with said one roll as it travels through an arc of about 180° and further wherein said extruded sheet remains in contact with said another roll as it travels through an arc of about 180 °.

Claim 12

The process according to claim 10, wherein said extruded sheet is passed through a cooling liquid bath after leaving said cooled smoothing calender.

Claim 13

The process according to claim 1, wherein said extruded sheet is passed through a cooling liquid bath after leaving said cooled smoothing calender.

Claim 14

The process according to claim 1, wherein said cooled smoothing calender is positioned such that the distance travelled by said extruded sheet as it passes from said nozzle to the point where said rib sheet tangentially engages said calender is about 2 to 10 cm.

Claim 15

The process according to claim 3, wherein said cooled smoothing calender is positioned such that the distance travelled by said extruded sheet as it passes from said nozzle to the point where said rib sheet tangentially engages said calender is about 2 to 10 cm.

Claim 16

The process according to claim 9, wherein said cooled smoothing calender is positioned such that the distance travelled by said extruded sheet as it passes from said nozzle to the point where said rib sheet tangentially engages said calender is about 2 to 10 cm.

Claim 17

The process according to claim 1, wherein said extruded sheet is horizontal as it passes between said slotted nozzle and said smoothing calender.

Claim 18

The process according to claim 2, wherein said extruded sheet is horizontal as it passes between said slotted nozzle and said smoothing calender.

Claim 19

The process according to claim 1, wherein said fixed rate is the same as the extrusion rate.

Claim 20

The process according to claim 3, wherein said fixed rate is the same as the extrusion rate.

Claim 21

The process according to claim 9, wherein said fixed rate is the same as the extrusion rate.

Claim 22

The process according to claim 1, wherein said extruded sheet is drawn through said cooled smoothing calender immediately after being extruded from said nozzle.

Claim 23

The process according to claim 21 further comprising winding up said unstretched bilaterally corrugated plastic sheet into a coil.

Claim 24

The process according to claim 3, wherein said extruded sheet is drawn off by said cooled smoothing calender immediately after being extruded from said nozzle.

Claim 25

The process according to claim 23 further comprising winding up said unstretched bilaterally corrugated plastic sheet into a coil.

Claim 26

The process according to claim 9, wherein said extruded sheet is drawn through said cooled smoothing calender immediately after being extruded from said nozzle.

Claim 27

The process according to claim 25 further comprising winding up said unstretched bilaterally corrugated plastic sheet into a coil.

Claim 28

The process according to claim 32, wherein said extruded sheet is drawn through said cooled smoothing calendar immediately after being extruded from said nozzle.

Claim 29

The process according to claim 27 further comprising winding up said unstretched bilaterally corrugated plastic sheet into a coil.

Claim 30

The process according to claim 1, wherein the rate of extrusion and the rate of drawing off are at a rate which ensures that no local acceleration and no elongation of the sheet occurs.

Claim 31

The process according to claim 1, wherein the extrusion rate from said nozzle is from 1-2 cm/sec.

Claim 32

A process for producing an unstretched bilaterally corrugated plastic sheet having a plurality of longitudinally extending parallel ribs on both sides thereof comprising extruding a plastic synthetic resin composition heated to a temperature above the melting point thereof from a wide band nozzle provided at its upper and lower sides in the flow direction with milled-in grooves to form an extruded sheet having longitudinally extending parallel ribs on both sides thereof, said ribs being arranged in exact opposition on each side of said sheet, drawing off the extruded heated sheet in the longitudinal direction of the ribs from said nozzle by conducting the sheet through a cooled smoothing calender, and cooling the extruded sheet within said calender to solidify said synthetic resin composition and thereby to form said unstretched bilaterally corrugated plastic sheet, said extruded sheet being drawn off from said nozzle at a fixed rate which is the same as or slightly more than the extrusion rate from said nozzle so that the ribs on said unstretched bilaterally corrugated plastic sheet exiting from said calender are uniform in size and shape, the height and width of the ribs being from about 1/15 to about equal to the thickness of a basic, non-ribbed, portion of the sheet and the basic, non-ribbed, portion of the sheet having a thickness of about 0.5 to 3 mm.

Claim 33

A process for producing an unstretched bilaterally corrugated plastic sheet having a plurality of longitudinally extending parallel ribs on both sides thereof comprising extruding a plastic synthetic resin composition heated to a temperature above the melting point thereof from a wide band nozzle provided at its upper and lower sides in the flow direction with milled-in grooves to form an extruded sheet having longitudinally extending parallel ribs on both sides thereof, said ribs being arranged in exact opposition on each side of said sheet, drawing off the extruded heated sheet in the longitudinal direction of the ribs from said nozzle by conducting the sheet through a cooled smoothing calender, and cooling the extruded sheet within said calender to solidify said synthetic resin composition and thereby to form said unstretched bilaterally corrugated plastic sheet, said extruded sheet being drawn off from said nozzle at a fixed rate which is the same as or slightly more than the extrusion rate from said nozzle so that the ribs on said unstretched bilaterally corrugated plastic sheet exiting from said calender are uniform in size and shape, the height and width of the ribs being from about 1/15 to about equal to the thickness of a basic, non-ribbed, portion of the sheet and the basic, non-ribbed, portion of the sheet having a thickness of about 0.5 to 3 mm.

Claim 34

The process according to claim 31, wherein said cooled smoothing calender comprises at least two parallel cylindrical rolls defining a nip therebetween, said sheet tangentially engaging the periphery of one of said rolls prior to passage of said sheet through said nip, said sheet tangentially engaging the periphery of another of said rolls after passage of said sheet through said nip.

Claim 35

The process of claim 32, wherein said sheet remains in contact with the periphery of said one roll as said one roll rotates through an arc of about 180°, and further wherein said sheet remains in contact with said another roll as said another roll rotates through an arc of about 180°.

Claim 36

The process of claim 31, wherein said cooled smoothing calender is positioned closely adjacent to said nozzle.

Claim 37

The process according to claim 31, wherein said cooled smoothing calender is positioned such that the distance travelled by said extruded sheet as it passes from said nozzle to the point where said rib sheet tangentially engages said calender is about 2 to 10 cm.

Claim 38

The process according to claim 32, wherein said cooled smoothing calender is positioned such that the distance travelled by said extruded sheet as it passes from said nozzle to the point where said rib sheet tangentially engages said calender is about 2 to 10 cm.

Claim 39

The process according to claim 31, wherein said extruded sheet is horizontal as it passes between said slotted nozzle and said smoothing calender.

Claim 40

The process according to claim 32, wherein said extruded sheet is horizontal as it passes between said slotted nozzle and said smoothing calender, and further wherein the arrangement of said cooled smoothing calender with respect to said slotted nozzle and the extent of cooling provided by said cooled smoothing calendar are so selected that said extruded sheet solidifies as it passes through said calender.

Claim 41

The process according to claim 31, wherein said fixed rate is the same as the extrusion rate.

Claim 42

The process according to claim 31, wherein said extruded sheet is drawn through said cooled smoothing calender immediately after being extruded from said nozzle.

Claim 43

The process according to claim 40 further comprising winding up said unstretched bilaterally corrugated plastic sheet into a coil.

Claim 44

The process according to claim 31, wherein said plastic synthetic resin is soft PVC.

Claim 45

A process for solidifying an extruded sheet passing out of an extrusion nozzle at an extrusion temperature, said extruded sheet having a plurality of longitudinally extending parallel ribs on both sides thereof, the ribs being arranged in exact opposition on each side of said sheet, which comprises conducting said extruded sheet immediately as it passes out of said extrusion nozzle through a distance of about 2 to 10 centimeters in the atmosphere to a cooled smoothing calender, and drawing the extruded sheet through the cooled smoothing calender, said extruded sheet engaging rolls of said calender in such a way that said extruded sheet is solidified by the time said extruded sheet passes through and separates from said calender, the ribs on said sheet being uniform in size and shape, with the height and width of the ribs being from about 1/15 to about equal to the thickness of a basic, non-ribbed, portion of the sheet and the basic, non-ribbed, portion of the sheet having a thickness of about 0.5 to 3 mm.

Claim 46

A process for solidifying an extruded sheet passing out of an extrusion nozzle at an extrusion temperature, said extruded sheet having a plurality of longitudinally extending parallel ribs on both sides thereof, the ribs being arranged in exact opposition on each side of said sheet, which comprises conducting said extruded sheet immediately as it passes out of said extrusion nozzle through a distance of about 2 to 10 centimeters in the atmosphere to a cooled smoothing calender, and drawing the extruded sheet through the cooled smoothing calender, said extruded sheet engaging rolls of said calender in such a way that said extruded sheet is solidified by the time said extruded sheet passes through and separates from said calender, the ribs on said sheet being uniform in size and shape, with the height and width of the ribs being from about 1/15 to about equal to the thickness of a basic, non-ribbed, portion of the sheet and the basic, non-ribbed, portion of the sheet having a thickness of about 0.5 to 3 mm.

Claim 47

The process according to claim 43, wherein said extruded sheet is comprises of soft PVC.

Claim 48

A process for the production of an unstretched bilaterally corrugated plastic sheet having a plurality of longitudinally extending parallel ribs on both sides thereof, said ribs being arranged in exact opposition on each side of said sheet and being approximately from about 1/15 to about equal to the thickness of an unribbed center portion of the sheet, comprising extruding a plastic synthetic resin composition in a horizontal plane from a slotted nozzle which is fashioned to be comb-like on both sides thereof, drawing off the extruded sheet in the longitudinal direction of the ribs from said slotted nozzle by conducting the sheet through a distance of from about 2 to 10 centimeters in the atmosphere to a cooled smoothing calender, and cooling and solidifying the extruded sheet within said calender to form said unstretched bilaterally corrugated plastic sheet, said extruded sheet being drawn off from said nozzle at a fixed rate which is the same as or slightly more than the extrusion rate from said nozzle so that the ribs on said unstretched bilaterally corrugated plastic sheet exiting from the calender are uniform in size and shape and the unribbed portion of the sheet having a thickness of about 0.5 to 3 mm.

Claim 49

A process for the production of an unstretched bilaterally corrugated plastic sheet having a plurality of longitudinally extending parallel ribs on both sides thereof, said ribs being arranged in exact opposition on each side of said sheet and being approximately from about 1/15 to about equal to the thickness of an unribbed center portion of the sheet, comprising extruding a plastic synthetic resin composition in a horizontal plane from a slotted nozzle which is fashioned to be comb-like on both sides thereof, drawing off the extruded sheet in the longitudinal direction of the ribs from said slotted nozzle by conducting the sheet through a distance of from about 2 to 10 centimeters in the atmosphere to a cooled smoothing calender, and cooling and solidifying the extruded sheet within said calender to form said unstretched bilaterally corrugated plastic sheet, said extruded sheet being drawn off from said nozzle at a fixed rate which is the same as or slightly more than the extrusion rate from said nozzle so that the ribs on said unstretched bilaterally corrugated plastic sheet exiting from the calender are uniform in size and shape and the unribbed portion of the sheet having a thickness of about 0.5 to 3 mm.