GB1574993A - Method of manufacturing foam insulated pipe - Google Patents

Description

(54) METHOD OF MANUFACTURING FOAM INSULATED PIPE (71) We, THE KENDALL COMPANY, a Corporation organised under the laws of the State of Delaware, of One Federal Street, Boston, Massachusetts, United States of America, do hereby declare the invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement: The present invention relates to a method of manufacturing foam insulated pipe.

Utilization of insulating jackets around pipes has long been employed in oil recovery and oil transportation. It is often necessary to heat the oil to be able to remove it from the ground and also to lower the viscosity for transportation through pipelines. In most geographical areas the temperature of the heated liquid can be maintained at the desired level only by insulating the pipe through which the oil flows.

Other uses of insulated pipe include natural gas recovery, water, steam and sewer pipes.

Many prior art techniques have been developed for enveloping a pipeline in a layer of foamed insulation. Some prior art techniques are characterized by said mold forming of the foamed insulating jacket although such a process is limited as to production capabilities and is accordingly expensive. Another prior art technique which has been utilized is to extrude the foamable liquid inside an eveloping jacket as the pipe lays in place in a ditch along the pipeline right of way. Machines have been developed for lifting the pipeline out of the ditch a sufficient distance to allow extrusion of the foamed insulating jacket and then replacement of the pipe into the ditch. Such an "over the ditch" process does not provide for optimum control over the cell structure and compressive strength of the end product.

Another prior art technique which has been attempted is to spray a foamable liquid onto the pipe as it is advanced longitudinally and rotated about its longitudinal axis. Such spray foaming techniques have heretofore suffered from an inability to accurately control the thickness of the foamed insulation as well as the cell structure and compressive strength of the final product.

It is a principal object of this invention to provide a method of handling pipes coated with foamed insulation which will avoid or mitigate damage to the coating.

According to one aspect of the present invention there is provided a methbd of manufacturing foam insulated pipe comprising the steps of applying foam to the pipe at a coating station; allowing the foam to rise and partially cure; providing a plurality of inflatable members for supporting the pipe, spaced in the direction of travel of the pipe away from the coating station, said members being inflated to a presure sufficient to support only a portion of the weight of the pipe and with the inflated pressure in each of said members increasing in the direction of travel of the pipe away from said coating station; moving the coated pipe onto said inflatable members and advancing the pipe along said members whereby that portion of the pipe which contacts those members closest to the coating station is supported to a lesser degree than that portion of the pipe which is farthest away from said coating station.

An embodiment of the present invention will now be described by way of exampIe with reference to the accompanying drawings wherein : Fig. 1 is a diagrammatic flow chart illustrating the steps involved in the coating of a pipe; Fig. 2 is a top plan view of the coating line wherein foamed insulation is applied to a pipe; Fig. 3 is an enlarged cross-sectional view taken along line 3-3 of Fig. 2; Fig. 4 is an enlarged elevational view looking in the direction of arrows 4-4 of Fig. 2; Fig. 5 is an enlarged perspective view of the spray head and wrapping station which form a part of suitable apparatus for applying a foamed insulative coating to a pipe; Fig. 6 is an enlarged cross-sectional view looking in the direction of arrows 6-6 of Fig. 2; Fig. 7 is an enlarged elevational view showing the manner in which the line of juncture between two lengths of pipe is marked; and Fig. 8 illustrates the manner in which two lengths of pipe are coupled together for application of the foamed insulative coating.

In its general aspect, the present invention contemplates a pipe to be covered with foam insulation will first be prepared by cleaning the surface to remove scale and dirt. This may be accomplished in a number of ways well known in the art including shot blasting, wire brushing, heating or some combination thereof.

It is desirable in most instances to provide a protective corrosion coating to the pipe surface before it is covered with foam insulation although this is not required for the present invention. The insulating foam may be applied directly to the bare pipe.

If a corrosion protective coating is applied, this may comprise any of the well-known coatings in the industry including tape, extruded coatings, coal tars, epoxies and other so-called thin mil coatings. Preferably, in order to provide for a continuous process, a number of pipes are coupled together in end-to-end relationship and advanced past the coating station. If for any reason, however, it is necessary to coat only a single length of pipe at one time, such a variance may be accomplished with the present invention.

A foamable liquid is sprayed onto the pipe which may or may not have previously been provided with a corrosion protective coating. The foamable liquid is applied to the pipe using one or more spray nozzles to distribute the liquid over a wide area, preferably at least 45 to 60 degrees (relative to a planar surface). In this manner only a small quantity of foamable liquid is applied to the pipe during any one revolution and, as the pipe continues to advance, the liquid foam rises into foamed insulation.

Various formulations for liquid foam may be utilized in the foaming process depending upon the desired density and cell structure of the end product. A particularly useful formulation is three pound density urethane foam utilizing freon as the blowing agent. It has been found that the foamable liquid used in the process should have a cream time, i.e., the time between the application and the time the foam begins to rise, of from 2 to 5 seconds. Full rise should occur between 4 and 30 seconds and the foamed layer should be capable of supporting its own weight (and the weight of the pipe) within about 45 seconds to no more than about 3 minutes.

After the foam has substantially risen, an outer layer of sheet material is wrapped around the foamed insulation to apply pressure to the rising foam to compact it and increase its density at the surface area above what it would be if the foam was allowed to rise uninhibited. This wrapping step is carried out between the time when rise of the foam is about 75% complete until within fifteen seconds subsequent to completion of the rise but while the foam is still deformable. The sheet material utilized for this purpose will vary depending upon the desired end product. If the sheet material is to also serve as an outer moisture barrier and provide additional corrosion protection for the pipe, a corrosion protective tape or extruded polyethylene or polypropylene type of coating may be employed. On the other hand, if the sheet material is not required to serve as a vapor barrier or is not intended to provide additional corrosion coating, a material such as fibreglass or its equivalent may be employed. In some instances, a material such as fiberglass is used and a corrosion protective coating or vapor barrier coating is sprayed, dipped, extruded, taped or otherwise applied over the sheet material. In any instance, however, the pressure applied through the sheet material should be sufficient to increase the density of the foam, at least in approximately the outer 25% of the total foam thickness, by about 10 to 25%.

To accomplish this end, the layer of sheet material should be applied from a point in time when the rise of the foam is about 75% complete to within 15 seconds subsequent to completition of the rise but while the foam is still deformable.

Another modification in the method is to treat the inner corrosion protective coating that is applied directly to the pipe electrostatically to bring about oxidation of the surface thereby promoting adhesion between the foam insulation and this inner coating. The foamable liquid itself may be e]ectrostatically sprayed to minimize waste and promote adhesion.

Still another nnodification of the process is to apply approximately 75 to 90% of the total thickness of the foam insulation desired in one application and allow this quantity to completely rise and partially set. A second spray head is then employed and positioned underneath the sheet material which is used to increase the density of the outer surface of the foam.

The remaining quantity of foamable liquid needed to complete the insulation layer is then sprayed beneath the sheet material as the latter is wound around the first thickness of foamed insulation. In this instance, the necessary pressure to increase the density of the foam insulation results almost entirely from the fact that the foam is caused to expand within a confined area.

In this alternative embodiment of the invention, it is desirable to use a foam of a higher density in the final layer to improve the structural strength of the insulating layer as a whole.

When the protective outer layer is applied after the sheet material is wrapped around the rising foam, various types of coatings may be employed. The outer layer may be sprayed, extruded, dipped or wrapped over the previously applied sheet material.

In the general aspect of the method of marking an object covered by foamable liquid, as described and claimed in copending application 40369/78 (Serial No.

1 574 992) there is applied to the object either ahead of or simultaneously with the foamable liquid a marking liquid characterized by undergoing vaporization at a temperature below the maximum temperature of the foam during the exothermic reaction which characterizes the rising. A suitable marking liquid is an organic solvent based paint which, in the case of pipe being covered with insulating foam, is sprayed onto the pipe immediately ahead of the foam.

The foamable liquid is allowed to rise, thus resulting in the foam rising to a greater degree at the point of application of the marking liquid because of vaporization of the latter during formation of the foam.

This will result in a ring of larger diameter than the main body of foam being formed in the foam insulation at the area where the marking liquid was applied.

The above method of marking employed is particularly useful in locating the ends of joints of pipes which have been coupled together to permit a continuous coating process but which need to be separated before shipping the pipe to the lay contractor. By using the method of the invention, the ends of the pipe may be quickly located and the insulating foam removed from the ends of the pipe for a distance to accommodate welding together.

Apparatus for handling pipe coated with foam employs a series of inflatable members adapted to be inflated to support a portion of the weight of a length of pipe without damaging the foam. Each member is of generally circular configuration and incudes a yieldable rubber-like material that presents a rounded outer surface. Two members are disposed in side-by-side relationship to present a carriage for supporting a portion of the weight of a length of pipe coated with foam.

A plurality of the inflatable members are disposed along the path of travel of a length of pipe and each successive member or pair of members is inflated to a slightly higher pressure so as to accommodate more weight of the coated pipe. Thus, the pipe handling method contemplates positioning inflatable members beneath the coated pipe and inflating the members to presssure sufficient to support only a portion of the weight of the pipe without damage to the foam insulation, and positioning a second inflatable member down-line from a first member and inflating the second member to a pressure greater than the pressure of the first member to support a greater weight yet still without damage to the insulative foam.

Referring initially to Figs. 1 and 2 of the drawings, a number of lengths of pipe 10, commonly referred to as "joints", are coupled together in end-to-end fashion and passed by a heating station 12 which utilizes a burner 14 to heat the surface of the pipe to the vicinity of 125"F., thereby driving off moisture and loosening some of the scale which may be on the pipe. Pipe 10 is advanced along its longitudinal axis while being rotated by a conveyor system comprising a plurality of pairs of rotating wheels 16 which are disposed in side-by-side relationship and slightly canted.

The pipe is advanced past a cleaning station 18 where a rotating wire brush 20 engages the surface of the pipe to remove dirt, rust and other contaminants.

Next, the pipe is wrapped with a corrosion protective layer of tape 22. Tape 22 is applied at a station 26 comprising a mounting standard 28 having spindles 30 for holding a first roll of tape 22m and a second roll of tape 22b. Tape 22 is threaded over a tensioning device 32 comprising a rotatable arm 33 which is retarded in rotation by a brake 34 and two stationary guides 36. Tape 22 is preferably a selfadhering resinous sheet. It normally includes a metal corrosion protective layer such as butyl rubber that is applied next to the metal and a layer of stronger, more structural, material such as polyethyene that serves as a carrier for the butyl and also acts as a vapor barrier. A particularly useful tape construction is one having a thickness of 13 mils including 9 mils of polyethylene and 4 mils of butyl rubber.

A wheel 38 mounted on an arm 40 rides along the layers of tape to hold pipe 10 in place. The tape is preferably applied in a helically wound pattern with 10 to 60% overlap.

To facilitate advancement of the pipe 10 in a longitudinal direction, the line of juncture between successive joints coupled in end-to-end relationship is taped for an area of several inches on either side of the juncture immediately after the pipe passes taping station 26. This coupling tape is indicated by the numeral 42 in the drawings and is preferably of a contrasting color to facilitate identification of the line of juncture when the foamed insulation is removed.

After the coupling tape has been applied, the pipe is advanced past a marking station 44 where an organic solvent base paint is sprayed onto the pipe through a nozzle 46.

Lines 48 and 50 leading from nozzle 46 bring the paint and air respectively to the nozzle. Nozzle 46 is operated periodically to apply the marking paint at the area where coupling tape 42 is wrapped around two succesive lengths of pipe with the paint preferably being applied in a narrow band 47 corresponding to the line of juncture.

Immediately after marking station 44, the pipe passes by a spray nozzle 52 to which a foamable liquid and a suitable blowing agent are directed through lines 54 and 56.

As best illustrated in Fig. 5, nozzle 52 is positioned in a horizontal plane at approximately the same level as the horizontal bisector of pipe 10 being coated. The foamable liquid is sprayed onto the pipe in a relatively wide band of 40 to 60 designated by the letter A in Fig. 5 so as to apply only a small quantity of foamable liquid to the pipe during any one revolution.

As the pipe continues to advance, the liquid foam rises into foamed insulation designated by the numeral 185 in Fig. 5. A ring gear 60 is formed in the foamed insulation at the area where marking paint 47 was applied.

After the foam has substantially risen, an outer layer of tape 61 is applied at a second taping station 62. Tape 61 is of the same type as tape 22 previously described except that it has properties enabling mechanical protection of the completed product. For example, tape 61 may comprise a total thickness of 25 mils with 20 mils of polyethylene and 5 mils of butyl rubber.

The tape 61 is pre-heated to about 120 135 F. at station 24. Taping station 62 comprises a standard 64 provided with spindles 66 for holding rolls of tape 61a and 61b. Tape 61 passes under a rotatable tensioning arm 68 before it passes onto the foamed insulation 58. Arm 68 is constructed in the same manner as rotatable arm 33 previously described including a brake 70 to provide the necessary tension on the tape 61.

It is important that sufficient tension be applied on tape 61 as it is wrapped around foamed insulation 58 to apply pressure to the risen foam to compact it and increase its density, in the outer one-fourth of its total thickness, above what it would be if the foam was allowed to rise uninhibited.

The pressure applied through tape 61 should be sufficient to increase the density by approximately 10% and preferably not more than about 25% in the outer 25% of the foam. The tape is wrapped around the foamed insulation in a spira pattern with 10% to 60% overlap to assure complete coverage.

The next step is to remove the foam insulation 58 for a distance back several inches from each end of the pipe being coated so as to allow adequate room for welding the pipe together as the pipeline is formed. This, of course, makes it mandatory that the line of juncture between successive joints of pipe which have been coated with the foamed insulation and wrapped with tape 61 be able to be located.

This is the function of marking ring 60 which projects outwardly to a greater circumference than the remainder of the coating on the pipe. Thus, the protective tape 61 and ultimately the foamed insulation 58 may be cut away from the pipe in the manner illustrated in Figs. 7 and 8.

Fig. 8 also illustrates the coupler 72 used to join two lengths of pipe in end-to-end relationship. A ferrule 74 of a diameter approximately equal to the internal diameter of pipes 10 is fitted in a tight friction fit within the pipe joints. A spacer 78 is disposed midway along the length of ferrule 74 to occupy the space between the ends of the two pipe joints 10.

As the coated pipe advances past the final taping station 62, it will be received by two inflatable wheels designated generally by the numerical 80 (Fig. 6). Each wheel 80 comprises a casing 82 of generally circular configuration mounted on a rim 84. Each casing 82 is formed from a yieldable rubberlike material with a relatively smooth rounded outer surface 86. Two members 80 are disposed in side-by-side relationship and canted slightly to achieve longitudinal advancement of the pipe while the members are rotating. To this end, each of the rims 84 is mounted on a shaft 88 with the end of the shafts being received in a pillow box bearing 90. A framework mounts the entire assembly in adlustably spaced relationship to the supporting surface.

Inflatable members 80 are filled with air to a pressure sufficient to support only a portion of the weight of the coated pipe without damaging the foamed insulation 58 or protective tape 61. The first pair of members 80 which receive the coated pipe as it emerges from the taping station 62 are inflated to a pressure sufficient to support only a portion of the weight of the pipe without damaging insulation 58 or tape 61.

Since this first set of inflatable members is supporting only a very small portion of the total weight of the coated pipe, the air pressure is relatively low. This of course is advantageous since the foam 58 is most susceptible to damage at this point since it is unlikely to be completely cured at that point. As the pipe advances further, the foamed insulation 58 will become more fully cured and, accordingly, the air pressure within the subsequent pairs of members 80 may be increased so that each pair of members 80 is capable of supporting a larger portion of the total weight of the pipe than the previous pair. This of course is advantageous since, as more of the weight of the coated pipe is placed on the members, it is necessary to have a higher pressure to support the pipe.

It has been found that a particularly useful liquid foam is three pound density urethane foam utilizing freon as the blowing agent. The liquid constituents are preheated to about 100 F. before reaching spray nozzle 52. The liquid is sprayed through an orifice of approximately .04 inch diameter at a pressure of from 600 to 2000 pounds per square inch. It has been found desirable to utilize a fan spray width (A in Fig. 5) of 40 to 60 degrees. For six to eight inch diameter pipe a forward speed of advancement between three and four inches per revolution is satisfactory to build up a foamed insulating layer of one to three inches in thickness.

The foamable liquid used in the process of the present invention should have a cream time, i.e., the time between application and the time the foam begins to rise, of from two to five seconds. Full rise should occur between four and thirty seconds and the foamed layer should be capable of supporting its own weight (and the weight of the pipe) within about fortyfive seconds to no more than about three minutes. The outer layer of protective tape may generally be applied from a point in time when the rise of the foam is about 75% complete to within 15 seconds subsequent to completion of the rise but while the foam is still deformable.

It will be appreciated that other modifications of the invention may be practiced without departing from the scope thereof which is intended to be limited only by the

Claims (3)

1. appended claims.

   Reference is made to co-pending Application No. 40484/77 (Serial No. 1 574 991) which claims the above described method of applying a foamable liquid to a cylindrical object and to co-pending Application No.

   40369/78 (Serial No. 1 574 992) which claims the above described method of marking a point on an object being covered by a foamable liquid.

   WHAT WE CLAIM IS: 1. A method of manufacturing foam insulated pipe comprising the steps of applying foam to the pipe at a coating station; allowing the foam to rise and partially cure; providing a plurality of inflatable members for supporting the pipe, spaced in the direction of travel of the pipe away from the coating station, said members being inflated to a pressure sufficient to support only a portion of the weight of the pipe and with the inflated pressure in each of said members increasing in the direction of travel of the pipe away from said coating station; moving the coated pipe onto said inflatable members and advancing the pipe along said members whereby that portion of the pipe which contacts those members closest to the coating station is supported to a lesser degree than that portion of the pipe which is farthest away from said coating station.
2. 2. A method of manufacturing foam insulated pipe as claimed in Claim 1 and substantially as hereinbefore described.
3. 3. A foam insulated pipe made by the method of claim 1 or claim 2.