Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
192 words
A process of extrusion-coating the central core, for use in a submarine coaxial cable for communication with alternating current signals having a maximum frequency of not less than 30 MHz, with an insulator of high pressure-produced polyethylene having a density of from 0.925 to 0.940 g/cm 3 and melt index of from 0.01 to 0.3 g/10 min, comprising the steps of: (a) extruding the central core covered with the insulator of polyethylene from an extruder, wherein a temperature of the polyethylene at the extrusion outlet is in the range of from 170° to 200° C; (b) just after extrusion into the atmosphere, immersing, and moving the extruded insulator-covered-core through a first group of at least one cooling water trough containing cooling water of a temperature which is in the range of from 80° to 100° C and is lower than the melting point of the polyethylene by a difference of from 10° to 30° C, thereby cooling the extruded insulator-covered-core gradually for about 10 to 30 minutes, and; (c) further, moving said insulator-covered-core through a second group of at least two cooling water troughs, thereby cooling the insulator-covered-core gradually to room temperature.
Claim 2
Dependent Claim
192 words
A process of extrusion-coating the central core, for use in a submarine coaxial cable for communication with alternating current signals having a maximum frequency of not less than 30 MHz, with an insulator of high pressure-produced polyethylene having a density of from 0.925 to 0.940 g/cm 3 and melt index of from 0.01 to 0.3 g/10 min, comprising the steps of: (a) extruding the central core covered with the insulator of polyethylene from an extruder, wherein a temperature of the polyethylene at the extrusion outlet is in the range of from 170° to 200° C; (b) just after extrusion into the atmosphere, immersing, and moving the extruded insulator-covered-core through a first group of at least one cooling water trough containing cooling water of a temperature which is in the range of from 80° to 100° C and is lower than the melting point of the polyethylene by a difference of from 10° to 30° C, thereby cooling the extruded insulator-covered-core gradually for about 10 to 30 minutes, and; (c) further, moving said insulator-covered-core through a second group of at least two cooling water troughs, thereby cooling the insulator-covered-core gradually to room temperature.
Claim 3
Dependent Claim
49 words
An extrusion-coating process according to claim 1, wherein said first group of cooling water troughs are arranged so that each trough except for the first one contains cooling water of a temperature lower than that of the neighbouring upstream trough by a difference of from 3° to 10° C.
Claim 4
Dependent Claim
22 words
An extrusion-coating process according to claim 1, wherein said insulator-covered-core passes through a first group of one to five cooling water troughs.
Claim 5
Dependent Claim
45 words
An extrusion-coating process according to claim 1, wherein the first trough in said second group of cooling water troughs contains cooling water of a temperature lower than that of the last trough in the first group by a difference of from 3° to 30° C.
Claim 6
Dependent Claim
49 words
An extrusion-coating process according to claim 1, wherein said second group of cooling water troughs are arranged so that each trough except for the first one contains cooling water of a temperature lower than that of the neighbouring upstream trough by a difference of from 3° to 30° C.
Claim 7
Dependent Claim
33 words
An extrusion-coating process according to claim 1, wherein the cooling time of said insulator-covered-core in said second group of cooling water troughs is entirely within the range of from 50 to 170 minutes.