This invention relates to the field of pipe joints. In particular, this invention relates to the field of manufacturing pipe joints and, in particular, the bell end for use in a pipe joint.
It is well known in the art that to extrude plastic pipes in an elongated cylindrical configuration of a desired diameter and then to cut the extruded pipe into individual lengths. Generally, the individual lengths are conveniently sized and suitable for handling, shipping and eventual installation at a location generally distant from the location where the plastic pipes are extruded. Each length of pipe is enlarged or “belled” at one end sufficiently to receive the adjacent next pipe section in order to create a pipe joint. The “belled” end of the pipe is thus enlarged to have a diameter larger than the diameter of the extruded pipe in order to receive the “spigot” end of the next adjacent pipe length. Generally, the larger inside diameter of the bell is formed sufficiently large to receive the spigot end of the next section of pipe with sufficient clearance to allow the application of packing, caulking, elastomeric gaskets or other sealing devices designed to prevent leakage of pipe joints.
In general, the bell end will have a transition phase where the bell transitions from the large diameter sufficient to receive the spigot end, to the standard diameter of the pipe as it was when it was originally extruded. This transition phase also acts as a pipe stop to prevent further insertion of the spigot end of the adjacent pipe. At present, bell ends have been created with the transition phase of generally 15° to 30°. This has been done for a number of reasons. One reason includes the fact that the bell ends have been formed using thermoforming. Thermoforming involves heating an extruded pipe in order to cause the pipe to become more elastic permitting it to be formed about a mandrel generally to have a different shape. It is generally difficult to form a transition phase of greater than 30° with thermoforming.
However, the prior art devices with the transition phase of 15° to 30° run the risk that the spigot or male end can be inserted past the transition phase in the belled end of the external pipe. This induces “hoop tensile stresses” in the external pipe. These types of stresses could result in pipe failure.
While it is known to have pipes with transition phases greater than 30°, such pipes are made from processes which are much more costly than thermoforming. Such processes include forming the pipe by casting, which is generally much more expensive because the entire pipe must be placed in a cast, or, a fitting must be cast for the end of the pipe. Other bell forming processes have included making pipes of thicker diameter and then machining a transition phase, such as by grinding, grooving or welding the pipe. The difficulty with this approach is that much more material is used for the pipe along the entire length in order to have a diameter at the bell end sufficient to permit machining of this type increasing the overall cost of the entire piping system. Furthermore, these processes tend to be much more expensive, both in the term of labour and time than thermoforming. Furthermore, these processes tend to require initial costs to implement the processes, such as for the equipment and/or the forms to cast the parts.
Accordingly, there is a need in the art for a pipe stop system having a bell end with a transition phase of greater than 30° that is not manufactured by machining or molding. There is also a need in the art for a method to manufacture a bell end having a transition range that decreases hoop tensile stresses, but which can be economically used on extruded pipe with a minimum of cost due to labour or additional materials.
Accordingly, it is an object of this invention to at least partially overcome some of the disadvantages of the prior art. Also, it is an object of this invention to provide an improved type of pipe joint having a bell end with a transition phase having a transition angle of preferably greater than 35° and more preferably greater than 45°. It is also an object of this invention to provide a method for forming a transition phase in the bell end with a transition angle of preferably greater than 55° and more preferably about 60°.
Accordingly, in one of its aspects, this invention resides in a process for thermoforming a bell end in an extruded thermoplastic pipe, said bell end having a transition angle at a transition phase of greater than 35° with respect to a longitudinal axis of the pipe, said process comprising: heating a first end of the extruded pipe; after heating, pushing the first end onto a mandrel, said mandrel extending along a longitudinal axis and having a working surface, said working surface having a first portion with an outer diameter corresponding to the inner diameter of the extruded pipe, a second portion having an outer diameter corresponding to the outer diameter of the extruded pipe, and a sloped portion intermediate the first portion and the second portion, said slope portion having at least one forming angle greater than 35°, said first end being initially pushed onto the first portion; after the first end has been fully pushed onto the mandrel, conforming the first end to the working surface of the mandrel; and after the first end has been cooled, removing the first end from the mandrel.
In a further of its aspects, this invention resides in a process for thermoforming a bell end with a transition phase of greater than 35° in an extruded thermoplastic pipe having a length, said process comprising: heating a first end of the extruded pipe; after heating, pushing the first end onto a mandrel in a first direction, said mandrel extending along a longitudinal axis and having a working surface with at least one forming angle greater than 35° with respect to the longitudinal axis and increasing an outer diameter of the mandrel in the first direction; after the first end has been fully pushed onto the mandrel, applying pressure to an outer surface of the first end to conform the first end to the working surface of the mandrel; and after cooling of the first end, removing the first end from the mandrel.
Accordingly, one advantage of the present invention is that the transition phase has a transition angle which is more than 35°, and more preferably will be greater than 45°, and still more preferably greater than 55°. In a preferred embodiment, the transition phase will have a transition angle of about 60°. It is understood that the transition angle of about 60° may not be consistent on the inside and outside of the pipe. For instance, with the transition phase of about 60°, the inner angle may be about 57°. Reference to the transition angle generally refers to the angle on the inside of the pipe.
It has been appreciated that by changing the angle of the transition phase from 30° to 60°, the radial resultant forces into the belled end of the external pipe are reduced substantially, such as by up to 40%, when inserting the spigot end. Furthermore, it has been appreciated that by increasing the transition phase from 30° to 60°, the radial stresses, also referred to as the hoop stresses, may be reduced by almost 50%. By reducing the resultant forces and radial stresses by about 40% and about 50%, respectively, the instances of failure of the pipe in the field can be greatly reduced. Accordingly, an improved pipe stop system to prevent over-insertion of the spigot end can be provided.
It is also understood that pipes will have maximum insertion lines indicating the length beyond which the spigot end should not be inserted. However, it is not rare that this maximum insertion line is not respected for a number of different reasons which will result in pipes being over-inserted thereby creating the hoop tensile stresses referred to above. The present invention provides an advantage over the prior art by reducing the radial resultant forces and the radial stresses even if the maximum insertion line is not respected. It is also understood that during installation, pipes may be compressed for a number of reasons. In such instances, even if the maximum insertion line is respected when the pipes are initially joined, later stresses may arise during installation. Accordingly, the present invention also provides advantages by removing resultant forces and radial stresses during insertion and installation.
It is also understood that the present invention can work with any type of thermoplastic extrusion pipe. However, it has been appreciated that in a preferred embodiment the present invention will operate particularly well with polyvinyl chloride (PVC) pipes.
Further aspects of the invention will become apparent upon reading the following detailed description and drawings, which illustrate the invention and preferred embodiments of the invention.
In the drawings, which illustrate embodiments of the invention:
Preferred embodiments of the invention and its advantages can be understood by referring to the present drawings. In the present drawings, like numerals are used for like and corresponding parts of the accompanying drawings.
It is not uncommon for the spigot end A to have a maximum insertion line, shown generally by reference numeral 7. However, it is also not uncommon that this maximum insertion line 7 is ignored for different reasons, such that the pipe A is over-inserted into the pipe B creating stresses that can lead to failure. In fact, the chamfer 9 of the socket end 1 may come into contact with the transition phase LT as best illustrated in
To prevent adverse effects caused by the over-insertion of the pipe A into the bell end 2 of the pipe B it is preferred if the transition phase LT have a transition angle α with respect to the longitudinal axis LA of at least 35°.
This is illustrated, for instance, in
It would appreciated that an “ideal” transition angle α of 90° will eliminate the entire radial resultant force. However, even transition angles α of greater than 35° have been found to decrease most of the destructive radial component forces Ry.
In order to thermoform a transition phase a of greater than 35° in a pipe 4, a mandrel 40, as shown in
The mandrel 40 also, preferably, has a working surface, shown generally by reference numeral 60. With reference to
Furthermore, in a preferred embodiment, the sloped portion 63 of the working surface 60 intersects the first portion 61 at a first longitudinal position LP1 along the longitudinal axis LM of the mandrel 40 and the sloped portion 63 intersects the second portion 63 at a second longitudinal position LP2 along the longitudinal axis LM of the mandrel 40. The sloped portion 63 is preferably sloped with respect to the longitudinal axis LM with the at least one forming angle β from the first longitudinal position LP1 to the second longitudinal position LP2. In this way, the sloped portion 63 has a generally inclined surface at the sloped angle β with respect to the longitudinal axis LM. In other words, the working surface 60 preferably is inclined at the sloped angle β with respect to the longitudinal axis LM over the sloped portion 63 corresponding to the axial position of the transition phase LMT along the axis L of the mandrel 40.
As illustrated in
This is illustrated in
After the first end 11 has been fully pushed onto the mandrel 40, the first end 11 is conformed to a profile substantially corresponding to the working surface 60 of the mandrel 40. This can be done in a number of ways, such as applying pressure to the outside of the pipe 4. Pressure can be applied either by air pressure or by physical pressure. This is illustrated, for instance, in
As indicated above, air holes 42 may be present in the mandrel 40 to avoid air becoming trapped between the pipe 4 and the mandrel 40, particularly along the sloped portion LMT. As illustrated in
In the further preferred embodiment, as illustrated in
Before the pipe 4 is pushed onto the mandrel 40, as illustrated in
To accomplish this, a preheater, as shown generally by reference numeral 600 in
Because the pipe 4 is on the conveyor 640 from the extruder, the preheater 600 may have a hinge, shown by reference numeral 660, upon which the upper portion 661 located above the dot-dash line 660 may rotate with respect to the lower portion 662 to facilitate insertion and removal of the pipe 4. In this way, the upper portion 661 may move upward in the direction Do to an open position (not shown) to permit insertion of the pipe 4 and then rotate downward in the direction DC to the closed position shown in
After the preheater 600, the pipe 4 is preferably inserted into a heating box, as shown generally as reference numeral 700 in
Each zone 701, 702 have top heaters 710. The top heaters 710 in each zone 701, 702 consist of twelve heating plates which measure 8″×8″ in dimension and consume up to 1,200 W of electrical energy each. The twelve heating plates 710 are arranged in three rows, 711A, 711B and 711C in the first zone 701 and three rows 712A, 712B and 712C in the second zone 702. The heating plates 710 heat the outside of the pipe 4. The temperature of each row 711A, 711B, 711C, 712A, 712B and 712C can be controlled independently. In a preferred case, the respective temperatures of each row 711A, 711B and 711C in the first zone 701 are about 980° F., 1060° F. and 130° F., respectively, and, the respective temperatures of each row 712A, 712B and 712C in the second zone 702 are 740° F., 1060° F. and 1300° F., respectively.
In addition to the top heater 710, the heating box 700 also comprises a plurality of pin heaters, as shown generally by reference numeral 742. The pin heaters 742 are arranged inside the pipe 4 when the first end 11 of the pipe 4 is inserted into an inserted position in the heating box 700 as illustrated by dashed lines in
As illustrated in
The other rods 760 of the plurality of rods 740 may be 18″ in length and each may have a second portion effective heating length of 9″, as shown generally by reference numeral 762, to heat the pipe 4 at the longitudinal position LH2 correspond to the second portion L2 of the pipe 4, when the pipe 4 is in the inserted position in the headers 701, 702. The heating rod 760 will generally be ¾″×12″ long and have an output of up to 2,000 W to heat the portion of the first end 11 that will fit over the second portion 62 of the working surface 60 of the mandrel 40 and form the second portion L2 of the bell end 2.
It has been appreciated that adding the extended rod 750 with the effective length 752 coinciding with the portion of the pipe 4 which will fit over the sloped portion 63 of the mandrel 40 and eventually form the transition phase LT of the bell end 2 facilitates formation of a transition angle α at the transition phase LT of the pipe 4 which is greater than 35°. It is also noted from
In general, the heating rods 750, 760 will not be heated to a particular temperature, but rather the temperature of the effective length 752, 762 of the rods 750, 760 will be controlled by controlling the percentage of power applied to the rods 742. In a preferred embodiment, the pipe 4 is 18″ DR25 and the power usage of the rods 742 is about 50% of the full capacity. It is understood that a person skilled in the art may modify these temperatures for different thickness of pipes so as to obtain the proper heating of the pipe 4 without burning or permanently damaging the pipe 4.
As indicated above, the first end 11 will be initially placed into the preheater 600 shortly after extrusion. This can be done for about 10 to 20 seconds depending on the extrusion process. The first end 11 is then placed in the first heating zone 701 in the heating block 700 for about 640 seconds and then may be placed in the second heating zone 702 for a further 640 seconds. The first end 11 will then be placed on the mandrel 40, and the process described above will take place to form the bell end 7. The time for heating the first end 11 in the preheater 600 and the heating box 700 will be selected to substantially correspond to the time required to extrude another length of pipe 4. Therefore, after this combined amount of time to thermoform a bell end 2 on a length of pipe 4, a further length of pipe 4 will have been extruded by the extrusion machine (not shown). Therefore, in general, the time required to extrude a length of pipe 4 substantially corresponds to the total time required to preheat the first end 11 in the preheater 600, heat the first end 11 in the heating box 700 as well as the time required to push the first end 11 onto the mandrel 400, conform the first end 11 to the working first surface 60 of the mandrel 40 by cooling the first end 11, and strip the first end 11 from the mandrel 40. This provides an efficient process for continuously forming lengths of pipe having a bell end 2.
To allow the pipes to be moved easily between the heating zones 701, 702, the heating box 700 has wheels 780 which may move on a track 790. The wheels permit the heating box 700 shown in
After the heating process, the first end 11 of the pipe, and more preferably the longitudinal position where the transition phase LT will be formed, will have an average temperature of preferably at least 100° F., more preferably 200° F. and still more preferably 300° F. It has been found that heating the pipe 4 to have these preferred temperatures will facilitate movement of the first end 11 of the pipe 4 onto the working surface 60 of the mandrel 40 having a sloped portion 63 with a forming angle β of more than 35°. In this way, the bell end 2 can be formed with the transition phase LT having a transition angle α greater than 35° with respect to the longitudinal axis LA. However, it will be understood that these preferred temperatures are not precise temperatures but rather may vary by +/−10%, and, it is also understood these preferred temperatures may also vary with the diameter and/or thickness of the pipe 4.
At step 404, once the first end 11 of pipe 4 is well heated, the first end 11 of pipe 4 can be pushed onto the mandrel 40 with the help of mechanical means (not shown). It is preferred that the mandrel knuckles are retractable knuckles 44 which are in the opened or extended position while the first end 11 of pipe 4 is pushed onto the mandrel 40. At step 405, once the first end 11 of pipe 4 has been fully pushed onto the mandrel 40, doors or clamps 47 of a pressure chamber 46 are closed and a pressure that is applied to the outside of the first end 11 of pipe 4 to help conform the first end 11 of pipe 4 to the working surface 60 of the mandrel 40. Preferably, the pressure applied is about 100 to 120 pounds per square inch (PSI). As indicated above, breathing holes 42 preferably located at the sloped portion 63 of the working surface 60 assure that air cannot be trapped between the first end 11 of pipe 4 and the mandrel 40. In a preferred embodiment, in addition to the pressure, cold water 49 may be sprayed onto the outside surface of the first end 11 of pipe 4 while in the pressure chamber 46 to cool off the first end 11 of pipe 4 and “freeze” the first end 11 of pipe 4 with the desired profile corresponding to the working surface 60 of the mandrel 40.
As shown in step 407 after a certain period of time, which will depend on the size of the pipe 4, the pressure applied at step 405 in the cooling procedure, the pressure chamber doors or clamps 47 are open and the retractable mandrel knuckles 44 are collapsed or retracted to permit the removal of the first end 11 of pipe 4 from the mandrel 40. In step 408, the first end 11 of pipe 4 is removed using a mechanical device, such as a stripper ring 48.
Accordingly, using the above method, an extruded pipe thermoplastic pipe 4 having a transition angle α at the transition phase LT greater than 35° may be formed. In the preferred embodiment, the extruded pipe 4 will be thermoformed using this process to form a transition angle α at the transition phase LT greater than 45°, and more preferably greater than 55° and still more preferably about 60°.
To the extent that a patentee may act as its own lexicographer under applicable law, it is hereby further directed that all words appearing in the claims section, except for the above defined words, shall take on their ordinary, plain and accustomed meanings (as generally evidenced, inter alia, by dictionaries and/or technical lexicons), and shall not be considered to be specially defined in this specification. Notwithstanding this limitation on the inference of “special definitions,” the specification may be used to evidence the appropriate ordinary, plain and accustomed meanings (as generally evidenced, inter alia, by dictionaries and/or technical lexicons), in the situation where a word or term used in the claims has more than one pre-established meaning and the specification is helpful in choosing between the alternatives.”
It will be understood that, although various features of the invention have been described with respect to one or another of the embodiments of the invention, the various features and embodiments of the invention may be combined or used in conjunction with other features and embodiments of the invention as described and illustrated herein.
Although this disclosure has described and illustrated certain preferred embodiments of the invention, it is to be understood that the invention is not restricted to these particular embodiments. Rather, the invention includes all embodiments, which are functional, electrical or mechanical equivalents of the specific embodiments and features that have been described and illustrated herein.