PEKK EXTRUSION ADDITIVE MANUFACTURING PROCESSES AND PRODUCTS
20200276760 ยท 2020-09-03
Inventors
- Timothy A. Spahr (Galesville, WI, US)
- Bruce Clay (Boyertown, PA, US)
- David S. LIU (Bala Cynwyd, PA, US)
- Julien JOUANNEAU (Bryn Mawr, PA, US)
Cpc classification
B33Y10/00
PERFORMING OPERATIONS; TRANSPORTING
B29C64/118
PERFORMING OPERATIONS; TRANSPORTING
B29C64/30
PERFORMING OPERATIONS; TRANSPORTING
B29K2271/00
PERFORMING OPERATIONS; TRANSPORTING
C08G2650/40
CHEMISTRY; METALLURGY
C08G65/46
CHEMISTRY; METALLURGY
B33Y70/10
PERFORMING OPERATIONS; TRANSPORTING
B33Y40/20
PERFORMING OPERATIONS; TRANSPORTING
International classification
B29C64/30
PERFORMING OPERATIONS; TRANSPORTING
B33Y10/00
PERFORMING OPERATIONS; TRANSPORTING
B33Y40/20
PERFORMING OPERATIONS; TRANSPORTING
B33Y70/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present invention is directed to material extrusion additive manufacturing processes, including fused filament fabrication, used to manufacture improved parts, devices, and prototypes using polyetherketoneketones (PEKK) and polyetheretherketones (PEEK). Using the improved processes of the invention, PEKK or PEEK polymer readily is 3D printed by FFF such that it crystallizes slowly enough during deposition for the resulting part to remain mostly or substantially amorphous during printing and thus have low percentage and/or more uniform shrinkage per layer and little to no warping from the base during print, and yet fast enough so that the resulting part crystallizes in post-print processing without substantial or any loss of its printed structure.
Claims
1. A material additive manufacturing process for forming a semi-crystalline article using a extrusion printing process comprising at least the following step: (i) extrusion printing a thermoplastic polymer composition comprising random PEKK copolymer and optionally one or more additives, said PEKK copolymer having a T:I ratio of between about 61:39 to 85:15, to produce an article with a weight percent crystallinity of 15% or less.
2. The material additive manufacturing process of claim 1 further comprising the step of heat treating said article from step 1 to produce a post printed article, whereby the post printed article's weight percent crystallinity is increased.
3. The material additive manufacturing process of claim 1 further comprising the step of heat treating said article from step 1 to produce a post printed article with a final weight percent crystallinity of greater than 15%.
4. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 wherein the random PEKK copolymer has an inherent viscosity in 96% sulfuric acid between about 0.5 and 1.5 dL/g.
5. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 wherein prior to post printing treatment, crystallinity of the article is maintained at about 5 weight % or less.
6. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 wherein, prior to post printing treatment said article is substantially amorphous or amorphous, and is crystallizable post printing.
7. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 wherein said PEKK copolymer has a crystallization half-time at 250 C. greater than or equal to about two (2) seconds and less than 1 minute.
8. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 wherein the printer chamber is maintained at a temperature less than the Tg of PEKK copolymer.
9. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 wherein the printer chamber is maintained at a temperature less than the PEKK copolymer's cold crystallization temperature as measured by DSC.
10. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 wherein the printer chamber is maintained at a temperature less than 160 C.
11. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 wherein the printer chamber is maintained at a temperature from about 60 C. and to about 120 C.
12. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 to produce an article with a Z direction tensile stress at yield or break greater than about 40% of the x-y direction tensile stress at yield or break.
13. The material additive manufacturing process for forming an article using a material extrusion printing process of claim 2 wherein said additional step of heating comprises a multistep temperature process.
14. The material additive manufacturing process for forming an article using the extrusion printing process of claim 1 wherein the thermoplastic composition further comprises fillers and/or additives selected from the group consisting of carbon fibers, glass fibers, carbon nanofibers, basalt fibers, talc, carbon nanotubes, carbon powders, graphite, graphene, titanium dioxide, pigments, clays, silica, processing aids, antioxidants, and stabilizers.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0015]
[0016]
[0017]
[0018]
[0019]
[0020]
[0021]
DESCRIPTION OF THE INVENTION
[0022] As used herein, an amorphous polymer refers to a polymer that does not present any measurable crystallinity by x-ray diffraction (XRD).
[0023] As used herein, HDT means heat deflection temperature, measured using DSC according to ASTM method D3418 with an applied force of 0.45 MPa.
[0024] As used herein, X, Y directions refers to directions parallel to the print plate and Z direction refers to the direction perpendicular to the print plate.
[0025] Polyetherketoneketone (PEKK) comprises units of the following formulas:
(ArX) and (Ar.sub.1Y)Formula I
wherein: [0026] Ar and Ar.sub.1 represent each a divalent aromatic radical and are preferably selected among 1,3-phenylene and 1,4-phenylene; [0027] X represents an electron-withdrawing group which is preferably a carbonyl group; and [0028] Y represents an oxygen atom.
[0029] The polyether ketone ketone comprises moieties of formula II A and of formula IIB:
##STR00001##
[0030] According to a preferred embodiment, the polyetherketoneketone comprises, consists essentially of, or consists of, of moieties of formula IIA and IIB. Among these polymers are especially preferred polyether ketone ketones that have a molar ratio of moieties of formula II A:moieties of formula IIB (also called T:I ratio) that is between about 61:39 and 85:15, and in some embodiments from about 65:35 to 80:20, in particular from about 68:32 to 75:25, and which preferably may be about 70:30.
[0031] Suitable polyetherketoneketones are available from under the brand name KEPSTAN polymers from Arkema Inc., King of Prussia, Pa., including the KEPSTAN 6000 and 7000 series polymers.
[0032] Alternatively, the polyetherketoneketone may comprise other aromatic moieties of the formula I above, notably moieties where Ar and Ar.sub.1 may also be selected from bicyclic aromatic radicals such as 4,4-diphenylene or divalent fused aromatic radicals such as 1,4-naphtylene, 1,5-naphtylene and 2,6-naphtylene.
[0033] In one embodiment of the invention, desirable properties are achieved by choosing a thermoplastic polymer composition comprising, consisting essentially of, or consisting of PEKK copolymer having a T:I ratio that is between about 61:39 and 85:15, in some embodiments from about 65:35 to 80:20, in particular from about 68:32 to 75:25, and which preferably may be about 70:30. Notably, the PEKK utilized in the thermoplastic polymer compositions of the invention is a random copolymer, in contrast to the block copolymer having segments having very different crystallization behavior as described in U.S. Pat. No. 9,527,242.
[0034] According to a preferred embodiment, the thermoplastic polymer composition comprises, consists essentially of, or consists of PEKK copolymer having a molecular weight such that its inherent viscosity in 96% sulfuric acid according to ISO 307 test method is between about 0.5 and 1.5 dL/g, preferably between about 0.6 and 1.2 dL/g, more preferably between about 0.7 and 1.1 dL/g.
[0035] The preferred compositions of the invention including those comprising, consisting essentially of, or consisting of PEKK, exhibit crystallization half times at 250 C. which are greater or equal to about 2 seconds and less than 1 minute, preferably between about 4 and 30 seconds, even more preferably between about 5 and 20 seconds. Crystallization half time at a given temperature is the time necessary for the material to develop half of its maximum crystallinity content, using x-ray diffraction.
[0036] Crystallinity of the polymer may be measured, e.g., by X-ray diffraction (XRD). Crystallinity of the polymer may also be measured, e.g., by differential scanning calorimetry (DSC). For instance, X-ray diffraction data may be collected with copper K-alpha radiation at 0.5 deg/min for two-theta angles ranging from 5.0 to 60.0. The step size used for data collection should be 0.05 or lower. The diffractometer optics should be set as to reduce air scattering in the low angle region around 5.0 two-theta. Crystallinity data may be calculated by peak fitting X-ray patterns and taking into account crystallographic data for the polymer of interest. A linear baseline may be applied to the data between 5 and 60.
[0037] In some embodiments of the invention, the thermoplastic polymer compositions further comprise fillers and/or additives, such as one or more of carbon fibers, glass fibers, carbon nanofibers, basalt fibers, talc, carbon nanotubes, carbon powders, graphite, graphene, titanium dioxide, pigments, clays, silica, processing aids, antioxidants, stabilizers, and the like. The thermoplastic polymer compositions may further comprise additives that can adjust or modify the thermal properties of PEKK, or any additive that can change polymer or polymer blend Tg, Tm (melt temperature), Tc (crystallization temperature), crystallization kinetics (speeding up or slowing down), melt viscosity, and chain mobility.
[0038] Material Extrusion Additive Process
[0039] For the material extrusion additive 3D printing processes of the invention, the thermoplastic polymer composition, polymer, copolymer, or filled polymer formulations used may be in the form of filaments or pellets, generally formed by extrusion, or may be in the form of powder or flakes.
[0040] Notably, the 3-D printing of this invention is not a laser sintering process. Instead, the compositions or resins may be 3D printed in an extrusion (for example, fused filament fabrication) style 3D printer, with or without filaments. For fused filament fabrication, the filaments may be of any size diameter, including from about 0.6 to 3 mm, preferably about 1.7 to 2.9 mm, more preferably diameters of about 1.7 mm and about 2.8 mm, even more preferably 1.75 mm, 2.85 mm or other sizes, measured with an unweighted caliper. The filaments may be extruded with any sized nozzle device that can extrude filament, pellets, powder or other forms of the thermoplastic polymer composition comprising PEKK or PEEK copolymer.
[0041] A device useful for material extrusion additive manufacturing generally comprises all or some of the following components: [0042] (1) consumable material in the ready to print form (filament, pellets, powder, flakes, or polymer solution as specified by the printer); [0043] (2) a device feeding the material to the print head; [0044] (3) one or more print heads with a nozzle that can be heated up or cooled to a specified temperature for extruding of the melted material; [0045] (4) a print bed or substrate which may or may not be heated, where the part is being built/printed; and [0046] (5) a build chamber surrounding the print bed and the object being printed which may or may not be heated or which may or may not be temperature controlled.
[0047] Generally, the extrusion printing process comprises one or more of the following steps: [0048] (1) feeding the thermoplastic polymer composition comprising PEKK or PEEK copolymer filament, pellets, powder, flakes, or polymer solution into a 3D printer, the parts of which may or may not be heated to one or more predetermined temperatures; [0049] (2) setting the computer controls of the printer to provide a set volume flow of material, and to space the printed lines at a certain spacing; [0050] (3) feeding the thermoplastic polymer composition comprising PEKK or PEEK polymer composition to a heated nozzle at an appropriate set speed which may be pre-determined; and [0051] (4) moving the nozzle into the proper position for depositing a set or predetermined amount of thermoplastic polymer composition comprising PEKK or PEEK polymer material; and [0052] (5) optionally adjusting the temperature of the build chamber.
[0053] In one embodiment, the feed into the printer has a low shear melt viscosity between about 100 and 2000 Pa.Math.s at 1 Hz at the printing temperature. The printer may be operated at room temperature, i.e. with no heated bed and/or heated build chamber. Alternatively, the bed and/or build chamber may be temperature controlled, and for example have a heated bed of about 50-200 C., preferably above about 90 C., more preferably above 120 C., even more preferably above 140 C. The heated bed may also be at about 160 C., or just under the Tg of the polymer or polymer blend.
[0054] In another preferred embodiment, the 3-D printer may be programmed to operate at 105 to 130% overflow. This means that the volume of thermoplastic polymer composition fed by the printer is higher than the calculated volume required for the 3-D article being formed. Overflow may be controlled to result in a denser and mechanically stronger part. Overflow also helps to compensate for shrinkage, while increasing the strength and mechanical properties of the printed article. The overflow can be set by at least two different methods. In the first method, the software/printer is set to feed a higher percent of material into the nozzle than would be normally needed. In the second method, the software/printer may be set to decrease the spacing between lines, and thus create an overlap in the lines, resulting in extra material being used to print the article.
[0055] Process parameters of the 3-D printer can be adjusted to minimize shrinkage and warping, and to produce 3-D printed parts having optimum strength and elongation. The use of selected process parameters applies to any extrusion/melt 3D printer, and preferably to filament printing (e.g. FFF).
[0056] The nozzle temperature is maintained at a temperature between about 335 C. to 425 C., preferably between about 350 C. to 400 C.
[0057] The print (head) speed may be between 0.5 to 8.0 in/sec (13 to 200 mm/sec).
[0058] In one embodiment the print speed, layer thickness, nozzle temperature, and chamber temperature is adjusted so that the part that is printed and before any further crystallization step takes place (such as for example by heating) is only partially crystallized, having a weight percent crystallinity of 15% or less, preferably at 10% or less, and more preferably at 5% or less. In another embodiment, the print speed, layer thickness, nozzle temperature, and chamber temperature is adjusted so that the part that is printed and before any further crystallization step takes place (such as for example by heating) is substantially amorphous or amorphous, and yet is crystallizable post printing.
[0059] Surprisingly, the inventor's discovered that printing with a build chamber temperature maintained at less than the polymer's or polymer blend's cold crystallization temperature (as measured by DSC), preferably at least 50 C. below the cold crystallization temperature, more preferably at least 80 C. below the cold crystallization temperature, to prevent the printed part from more fully or fully crystallizing during print.
[0060] In another embodiment, the build chamber during printing may be operated at temperatures between about 18 C. (room temperature) to a temperature maintained at less than the polymer or polymer blend Tg (as measured by DSC), or between 40 C. (absolute) and 20 C. below Tg, or between 60 C. (absolute) and 40 C. below Tg.
[0061] In yet another embodiment, the build chamber (or print area) may be operated at temperatures between about 18 C. to 280 C., or between about 35 C. to 220 C., or between about 60 C. to 160 C., or between about 70 C. to 130 C.
[0062] In yet another embodiment, the build chamber (or print area) is operated and maintained at a temperature less than 160 C., preferably less than 140, more preferably less than 120 C.
[0063] In yet another embodiment, the build chamber (or print area) is operated and maintained at a temperature from about 60 C. and to about 120 C., preferably from about 60 C. and to about 100 C.
[0064] An advantage of the present invention is the ability to print less warping, stronger parts/devices/articles with better dimensional stability (after post print treatment using for example annealing), while printing at lower build chamber temperatures (for example, less than 160 C.) compared to other PAEK materials. Moreover, the lower build chamber temperature does not require sophisticated design, materials, and heat management systems, lowering overall printer cost.
[0065] In addition, the process may take place in air, or under an inert gas such as nitrogen. The printing process may occur at atmospheric pressure or under vacuum.
[0066] The thickness of each print layer may be about 0.004 inches (0.10 mm) to 0.1 inches (4 mm).
[0067] Description of Exemplary Post Printing Processing
[0068] Another advantage of the invention, typically not achieved with other materials and processes, is adjustment of polymer crystallization rates by way, for example, of T:I ratio of PEKK such that the printed percent crystallinity may be further modified during post printing processing/crystallization steps.
[0069] The process of the invention further includes the step of heat treating the article produced by the extrusion printing step to provide a post printed article having increased crystallinity (weight percent), compared to the weight percent crystallinity of the article produced by the extrusion printing step and pre-heat treatment.
[0070] After printing, the resulting 3-D articles may be placed in an oven (with or without oven time temperature programmability) at a temperature time period to be specified or which is predetermined to increase the part's/article's percent crystallinity, mechanical properties, and its temperature of use, while preserving the strength of the polymer's interlaminate adhesion (also called the Z direction strength). This crystallization step may be done at a temperature above the polymer's Tg (for example, for PEKK, 160 C.-165 C.). It also can be done on parts with an initial 2% to 98% of the polymer's possible crystallinity. Optionally, the post treatment process could occur by increasing the build chamber temperature after the printing process has been completed without removing the part from the build chamber.
[0071] The post printing crystallization temperature may be between a temperature of about 160 C. to 320 C., or between about 180 C. to 290 C., or between about 220 C. to 290 C., or between 200 C. to 250 C. The time period for the post printing crystallization process is/are single or multiple temperature steps having a duration between about 1 minute and 24 hours, preferably between about 3 minutes and 3 hours, more preferably between about 10 minutes and 60 minutes per temperature step. Post printing crystallization may also comprise the step of heating past the point the part reaches maximum crystallinity, up to, for example, 24 hours.
[0072] Preferably, post printing crystallization is a multistep temperature step process. In one embodiment of the multistep temperature process, the first step is at about 150-170 C., or at about 160-165 C., for about 30 minutes to 3 hours, or from about 1 to 2.5 hours, or for about 1 hour; the second step being at about 180-240 C., or from about 200-230 C. for about 30 minutes to 3 hours, or from about 1 to 2.5 hours, or for about 1 hour. Using the processes of the invention, a post printed article with a final weight percent crystallinity of greater than 15%, preferably 20% or greater, more preferably about 25% or greater, most preferably at least 30% or greater, up to about 35%, was produced. Depending on part size and geometry, the time for both the first and second steps can be optimally scaled to accommodate larger parts.
[0073] In one embodiment post printing crystallization comprises heating and equilibrating the printed part to a temperature within about 10 C. of the Tg of the polymer or polymer blend and then slowly heating to the crystallization temperature. This slow, multi stage heating cycle reduces distortion during crystallization that might otherwise occur if the printed part was heated quickly and unevenly.
[0074] Upon printing and before any post printing heating steps, the part/article of the invention which is a semi-crystalline article comprising PEKK copolymer will have an elongation and yield strength when printed and tested in the XY direction that is similar to that of an injection molded article of the same composition, maintaining over about 40%, 50%, 60%, 70%, 80%, 90% or more, and in some cases over about 95% of the stress at yield of the part/article of the same composition made by injection molding. Likewise, post printing and after further heat treatment to increase crystallization, the part/article of the invention which is a semi-crystalline article comprising PEKK copolymer will have an elongation and yield strength when printed and tested in the XY direction that is similar to that of an injection molded article of the same composition, maintaining over about 50%, over about 75%, preferably over about 85%, and in some cases over about 95% of the stress at yield of the part/article of the same composition made by injection mold. In addition, the Z direction stress at yield will average greater than about 20%, preferably greater than about 30%, more preferably greater than about 40%, 50%, 60%, 70%, 80%, 90% or more, of the stress at yield in the XY direction of the part without filler.
[0075] In one embodiment, the article produced using PEKK has a Z-direction tensile stress at yield or break greater than about 40% of the x-y direction tensile stress at yield or break.
[0076] By contrast, articles comprising PEEK polymer (used per se, without additives) printed in the extrusion printing process yields a Z direction stress at yield averaging less than 10% of the stress at yield in the XY direction of the part without the addition of fillers at similar print conditions.
[0077] In one embodiment, the present invention provides a material comprising a single PAEK composition, such as PEKK, yielding parts with a HDT above about 200 C., preferably about 250-260 C., and a Z direction tensile stress at yield or break greater than 40% of the x-y direction tensile stress at yield or break. PEKK copolymer having a 60:40 T:I ratio material has a HDT of less than 160 C. The inclusion of fibers or other reinforcements may further increase the HDT of a finished article.
[0078] Thus, for each thermoplastic polymer composition of the invention comprising PEKK or PEEK polymer, depending on its crystallization rate and T:I ratio (to the extent there is one), there is a build chamber temperature in which temperature is determined and optimized such that the part/article/device surprisingly prints substantially or mostly amorphous. For example, for PEKK having a T:I ratio of 70:30, that temperature is about 90 C. Any hotter, and the part starts becoming unacceptably crystalline during printing. This finding is counter to previous understandings that the favored higher build chamber temperatures.
[0079]
[0080]
[0081]
[0082] The processes of the invention can also provide near net shapes by, for example, printing a slightly oversized part, crystallizing it, and then machine or cutting the part to the desired shape, including for example drilling of holes.
EXAMPLES
Example 1
[0083] Filament 1.75 mm in diameter was prepared by extrusion with samples PEKK (1) and PEKK (2), having T:I ratios of 60:40 and 70:30 respectively. PEEK filament 1.75 mm in diameter was purchased from Essentium Inc. Filament prepared with PEKK (1) and PEKK (2) was transparent, indicating that the polymer was substantially amorphous. The PEEK filament was opaque, suggesting at least some degree of crystallinity. Modified ASTM D638 Type IV tensile bars were created in a FFF process in both a horizontal and vertical orientation. For all materials, a 0.4 mm diameter nozzle and 0.2 mm layer height was used. PEKK (1) was printed using an extruder temperature of 360 C., PEKK (2) at 375 C. and PEEK at 420 C. PEEK was printed at a higher temperature than PEEK (2) despite its lower melting point because at lower temperatures layer adhesion was too poor to complete a print. A chamber temperature of 75 C., and heated bed of 160 C. was used for all prints. The specimens printed in the horizontal direction have the raster orientation oriented in alternating directions 45 from the testing direction. The vertical orientation direction samples directly measure the layer adhesion. Half of the PEKK tensile specimens were crystallized by heating in an oven to 160 C. for one hour, followed by 200 C. for one hour. The tensile strength was measured according to ASTM D638 standards, and the crystallinity was measured by WAXD.
[0084] Results are report in Table 1 Specimens printed with PEKK (1) filament showed little or no increase in crystallinity during this crystallization cycle, and samples prepared in the vertical orientation distorted during the crystallization cycle and could not be tested. Tests with PEKK (2) show that with the appropriate T:I ratio and printing conditions, it is possible to produce a mostly amorphous part that can be crystallized in a secondary process to increase its strength. Parts printed with PEKK (2) at high build chamber temperatures had significant distortions and poor layer adhesion. During the crystallization process, parts shrink uniformly and predictably 2.5% in the x and y axis and about 0.5% in the z axis.
[0085]
TABLE-US-00001 TABLE 1 Crystallinity (wt. % via XY maximum XY elongation Z maximum Z elongation WAXD) stress (MPa) to break (%) stress (MPa) to break (%) PEKK as printed 0% 83 10.4% 48 5.5% (1) PEKK post 0% 87 11.0% n/t n/t (1) treatment PEKK as printed 0-2.5%.sup. 84 13.0% 51 4.8% (2) PEKK post 22% 90 8.2% 56 5.2% (2) treatment PEEK as printed 21% 79 19.9% 5 5.0%
Example 2
[0086] To measure distortions while printing, a long narrow item was printed about the width of two extrusion passes (0.8 mm), about 1 cm tall, and 4 cm long with the printing and crystallization conditions used in Example 1. The percent difference in dimension on the long axis of the printed part (taken in the shortest section) compared to the specified, theoretical length (4 cm) was measured as a way to quantify layer distortion/shrinkage during printing. Table 2 list the percent shrinkage measured for PEEK (2) as printed, PEKK (2) crystallized, PEEK as printed, and an acrylonitrile butadiene styrene amorphous polymer (ABS). The results show that PEKK has shrinkage similar to a typical ABS and substantially less than PEEK while printing. Upon crystallizing through the post-process step, the PEKK (2) part experiences further, but uniform shrinkage.
TABLE-US-00002 TABLE 2 Shrinkage Data Material % Distortion on Thin Wall PEKK (2) as printed 1.2% PEKK (2) after post-processing 3.0%* uniform shrinkage PEEK as printed 4.4% ABS 1.1% *Uniform shrinkage
Example 3 (Modeling Example)
[0087] A finite element model tracking temperature and crystallinity was constructed to predict the internal and external crystallinity of a simple 3D printed PEKK 70:30 part consisting of 10 vertically stacked layers that are each 160 mm long, 0.4 mm wide, and 0.2 mm thick. The geometry used by the finite element model of this example is shown in
[0096] Crystallinity within the 3D printed part was derived from the time-temperature-transformation (TTT) diagram of PEKK 70:30 referenced in [Choupin, Mechanical performances of PEKK thermoplastic composites linked to their processing parameters (2017)], itself derived from differential scanning calorimetry (DSC) data. The TTT diagram describes the build-up of crystallinity based on time in minutes spent at a fixed annealing temperature. The spatially dependent temperature data predicted by the finite element model was used to predict the incremental rate of crystallization.
[0097]
[0098] The average crystallinity of parts printed between 40-240 C. as shown in
[0099]
[0100] Within this specification embodiments have been described in a way which enables a clear and concise specification to be written, but it is intended and will be appreciated that embodiments may be variously combined or separated without parting from the invention. For example, it will be appreciated that all preferred features described herein are applicable to all aspect of the invention described herein.
[0101] Numerous variations, changes and substitutions will occur to those skilled in the art without departing from the spirit of the invention. Accordingly, it is intended that the appended claims cover all such variations as fall within the spirit and scope of the invention.