Method of producing a thermoplastic polymer-lined pipe

Claim 2

A process for lining a pipe with a thermoplastic polymer which comprises: (a) selecting a substantially non-crosslinked, thermoplastic tubular polymer liner, the liner being heat shrinkable along its length and heat expandable in its diameter to provide a diametric expansion on heating about from 8 to 15%, the liner having an outside diameter less than the internal diameter of the pipe and which, when fully expanded, would have an outside diameter greater than the internal diameter of the pipe;

Claim 3

(b) inserting the tubular polymer liner into the pipe; and (c) heating the polymer liner sequentially from one point toward at least one free end of the pipe and uniformly about its circumference to a temperature sufficient to cause the liner to expand while applying a compressive axial force sufficient to overcome the drag forces of the liner, the compressive axial force being applied to the end of the liner toward which the liner is being heated.

Claim 4

(b) inserting the tubular polymer liner into the pipe; and (c) heating the polymer liner sequentially from one point toward at least one free end of the pipe and uniformly about its circumference to a temperature sufficient to cause the liner to expand while applying a compressive axial force sufficient to overcome the drag forces of the liner, the compressive axial force being applied to the end of the liner toward which the liner is being heated.

Claim 5

A process of claim 1 wherein the expandable polymer liner is prepared by (a) selecting a substantially non-crosslinked, thermoplastic tubular polymer liner of outside diameter greater than the internal diameter of the pipe; (b) heating the tubular polymer liner to within the normal annealing temperature range of the polymer and stretching the heated polymer liner until its outside diameter has been sufficiently reduced so that upon cooling to room temperature and subsequently relieving the tension the outside diameter of the liner is less than the internal diameter of the pipe.

Claim 6

A process of claim 1 wherein the axial pressure is equal to about from 100 to 400 pounds per square inch of the cross-sectional area of the pipe wall.

Claim 7

A process of claim 1 wherein the polymer liner is uniformly heated by passing therethrough an apparatus having anterior and posterior ends and comprising: (a) a platform; (b) at least one radiant heating element mounted on the platform; (c) a spiral air tube mounted on the platform to encircle the heating element at least once in a direction axial to the liner, the air tube having a plurality of apertures formed therein positioned to create a circumferential air flow within the pipe; (d) electrical and pressurized air sources functionally connected to the radiant heating element and air tube, respectively; (e) means for moving the platform through the pipe; and (f) a diametric gasket positioned anterior to the heating element to separate the apparatus from the portion of the pipe anterior to the heating element; while heating the element to a temperature of at least about 1200° F. and forcing gas through the air tube to provide a flow sufficient to distribute the heat substantially uniformly about the circumference of the liner.

Claim 8

A process of claim 4 wherein the apparatus is drawn through the pipe.

Claim 9

A process of claim 1 wherein successive sections of liner are joined by (a) circumferentially compressing the end of each stretched liner section to be joined about from 1 to 5% by clamping each such end with a circumferential clamp; (b) positioning the clamps to permit the ends of each liner section to protrude from the edge of each clamp about from 0.5 to 1.5 times the thickness of the liner; (c) heating the ends of the liner sections to be joined to the fusion temperature of the thermoplastic from which the liner is made; and (d) bringing the ends of the heated liner section into contact under pressure and maintaining the contact and pressure until the temperature of the ends falls to substantially ambient temperature.

Claim 10

A process of claim 1 wherein the stretched liner is heated in the presence of an inert gas.

Claim 11

A process of claim 1 wherein the pipe has a coating of about from 10 to 100 mils on the outer surface thereof of a thermoplastic elastomer, the thermoplastic elastomer having a flexural modulus of about from 500 to 10,000 psi, and a melt softening range of about from 40° to 120° C.