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US4345962A Expired / Lapsed US ⏱️ 0.0 years remaining

Control in application of pulp insulation to electrical conductors

Assignee: Nortel Networks Ltd
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Filing: 1981-06-25
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Granted: 1982-08-24
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Expires: 2001-06-25
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Abstract

Abstract Apparatus for applying pulp to a conductor with a control to operate an adjusting means to vary the amount of pulp fibre in a pulp bath dependent upon signals received corresponding to weight of pulp applied to the conductor whereby the weight is controlled within preset limits. Another requirement is an oven with at least two zones and a moisture measuring and diameter measuring means for pulp issuing from the oven, the latter means controlling the oven zone temperatures to provide a controlled degree of pulp expansion during flash evaporation and a controlled moisture retention in the dried pulp.

Inventors

  • 👤 William E. Cowley
  • 👤 Michael A. Shannon
  • 👤 Victor L. LeNir

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 07:23
CPC Classifications
H; H01; H01B; H01B13/00; H01B13/06; H01B13/12

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 248 words
Apparatus for pulp insulating a plurality of conductors comprising: a pulp bath for simultaneous passage of the conductors along side-by-side paths; weight measuring means to measure the weight of wet pulp applied to the conductors; means to adjust the amount of pulp fibre entering the bath per unit time; control means, actuable by signals received from the weight measuring means and corresponding to the actual weight of pulp per unit length, to operate the pulp fibre amount adjusting means to change the amount of the pulp fibre in the bath and thus to bring the weight within preset limits; an oven for drying the pulp, said oven being composed of at least two zones, an upstream zone and a downstream zone, said zones each having an adjustable drying temperature setting; a moisture measuring means and a diameter measuring means downstream of the oven to measure moisture retention and average final diameter of the pulp on the conductors; the diameter measuring means being associated with the adjustable temperature setting of the upstream zone of the oven to influence that setting to control the rate of flash evaporation in the upstream zone and thus the degree of expansion of the pulp during flash evaporation; and the moisture measuring means being associated with the adjustable temperature setting of the downstream zone of the oven to control the rate of drying in the downstream zone to provide a desired moisture retention in the pulp upon the insulated conductors emerging from the oven.
Claim 2
Dependent Claim 248 words
Apparatus for pulp insulating a plurality of conductors comprising: a pulp bath for simultaneous passage of the conductors along side-by-side paths; weight measuring means to measure the weight of wet pulp applied to the conductors; means to adjust the amount of pulp fibre entering the bath per unit time; control means, actuable by signals received from the weight measuring means and corresponding to the actual weight of pulp per unit length, to operate the pulp fibre amount adjusting means to change the amount of the pulp fibre in the bath and thus to bring the weight within preset limits; an oven for drying the pulp, said oven being composed of at least two zones, an upstream zone and a downstream zone, said zones each having an adjustable drying temperature setting; a moisture measuring means and a diameter measuring means downstream of the oven to measure moisture retention and average final diameter of the pulp on the conductors; the diameter measuring means being associated with the adjustable temperature setting of the upstream zone of the oven to influence that setting to control the rate of flash evaporation in the upstream zone and thus the degree of expansion of the pulp during flash evaporation; and the moisture measuring means being associated with the adjustable temperature setting of the downstream zone of the oven to control the rate of drying in the downstream zone to provide a desired moisture retention in the pulp upon the insulated conductors emerging from the oven.
Claim 3
Dependent Claim 71 words
Apparatus according to claim 1, wherein the diameter measuring means is also associated with the temperature setting of the downstream zone of the oven, a combining means being provided and connected to combine input signals received from the diameter measuring means and from the moisture measuring means to provide an output combined signal which is influenced by the input signals and for control of the temperature setting of the downstream zone.
Claim 4
Dependent Claim 59 words
Apparatus according to claim 2, wherein the oven has an intermediate zone between the upstream and downstream zones, said intermediate zone having an adjustable drying temperature setting, the moisture measuring means being associated with the adjustable temperature setting of the intermediate zone, to influence that setting to desirably affect the rate of evaporation of moisture in the intermediate zone.
Claim 5
Dependent Claim 94 words
Apparatus according to claim 2 provided with a means for measuring line speed and another combining means connected to combine signals received from the diameter measuring means and from the moisture measuring means to provide an output combined signal which is influenced by the input signals to adjust the pulp valve setting as required towards achieving a desired diameter of the insulation on each conductor and its moisture content consistent with a weight of pulp as applied to the conductors and as controlled by the weight measuring means in conjunction with the control means.
Claim 6
Dependent Claim 136 words
Apparatus according to claim 1, wherein the upstream zone of the oven has a manual temperature setting to automatically control the temperature of said zone, a comparator provided to compare a signal corresponding to the average diameter of the pulp on the conductors and a signal corresponding to the manually set temperature and to give an output compared signal, a controller means to read the actual temperature of the upstream zone and to transmit a signal to the controller corresponding to said actual temperature, and the controller connected to the comparitor to receive the output compared signal from the comparator and to compare it with the signal corresponding to the actual temperature to give an output control signal to adjust the temperature setting of the upstream zone as required to control the rate of flash evaporation.
Claim 7
Dependent Claim 127 words
Apparatus according to claim 2, wherein the downstream zone has a manual temperature setting to automatically control the temperature of said zone, a comparator provided to compare the output combined signal from the combining means and a signal corresponding to the manually set temperature and to give an output compared signal, a differentiator, means to read the actual temperature of the downstream zone and to transmit a signal to the differentiator corresponding to said actual temperature, and the differentiator connected to the comparator to receive the output compared signal from the comparator and to compare it with the signal corresponding to the actual temperature to give an output control signal to adjust the temperature setting of the downstream zone as required to control the rate of drying.
Claim 8
Dependent Claim 113 words
Apparatus according to claim 1, wherein the diameter measuring means comprises a scanning device movable across the paths of the conductors, said scanning device having a signal emitter and a signal receiver disposed on opposite sides of said paths to transmit signals across the paths and receive signals so transmitted for each conductor in turn, received signals corresponding to the diameter of an associated conductor, a comparator to compare the received signals with a datum indicative of the desired diameter of each conductor and to give an output compared signal, and means to store and average said compared signals to provide an output averaged signal to influence the setting of the upstream zone.

References Cited (Backward Citations)

US3779843A Cited
US4218285A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-08-23 1986-02-22 1986-08-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-08-23 1990-02-22 1990-08-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-08-23 1994-02-22 1994-08-24 $7700.00 Window Closed / Lapsed

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