Technical Field
This invention generally relates to gels having tack-free coatings and, more specifically, to methods for manufacturing gels having a permanent tack-free coating. Such gels are particularly useful when incorporated into surgical devices such as access ports.
Description of the Related Art
A “gel” is often defined as a semisolid condition of a precipitated or coagulated colloid. Despite its derivation from the Latin word gelare “to freeze,” gels differ widely in their fluid/solid characteristics, ranging from more fluid gels, such as those found in gel toothpastes, to more solid gels, such as those used in bicycle seat pads.
Gels tending toward the “solid” end of the spectrum are commonly used to facilitate load distribution. Gels enhance this function by offering a high degree of compliance, which basically increases the amount of area available to support a load. With an increased area of support, the load is accommodated at a considerably reduced pressure. Particularly where the human body is involved, a reduced pressure is desirable in order to maintain capillary blood flow in body tissue. It is with this in mind that gels are commonly used for bicycle seats, wrist pads, insole supports, as well as elbow and shoulder pads.
Gels have been of particular interest in the formation of seals, where the high compliance and extensive elongation of the gel are of considerable value. Such is the case with seals used in trocars and other surgical access devices, including access ports, in which a seal must be formed both in the presence of a surgical instrument (or surgeon's hand) and in the absence of a surgical instrument.
In general, an access device is a surgical device intended to provide access for surgical instruments across a body wall, such as the abdominal wall, and into a body cavity, such as the abdominal cavity. Often, the body cavity is pressurized with a gas, typically carbon dioxide, to enlarge the operative volume of the working environment. Under these conditions, the access device must include appropriate seals to inhibit loss of the pressurizing gas, both with and without a surgical instrument disposed through the seal. Seals formed from a gel material provide a high degree of compliance, significant tear strength and exceptional elongation and thus are particularly useful in access ports.
While the advantageous properties of gels have made them candidates for many applications, one disadvantage has seriously limited their use. Most gels are extremely tacky. This characteristic alone makes them difficult to manufacture and aggravating to use.
Attempts have been made to produce gels that are naturally non-tacky. Such naturally non-tacky gels, however, are not particularly heat tolerant, as low amounts of heat can rapidly cause the materials to take a set and distort, particularly under compressive loads. This can occur over an extended period of time, for example, even at normal room temperatures.
Attempts have been made to enclose tacky gels in a non-tacky pouch. This has also tended to mask the advantageous properties and to significantly increase manufacturing costs.
Lubricants such as silicone oil have been applied to the surface to reduce tackiness. Unfortunately, these lubricants tend to dry out over time leaving the gel in its natural tacky state.
Powders, including starch, have been applied to the tacky surfaces with results limited in both duration and effect. In addition, the use of a starch based powder as a blocking agent and the application of the blocking agent during production increases the cost of manufacture and may necessitate additional cleaning steps, greatly increasing the manufacturing time for producing powdered gel products.
Starch blocking agents further complicate manufacturing by providing a growth medium for bacteria and other microorganisms. Medical devices incorporating gels are typically irradiated at a higher than normal sterilization dose to compensate for this. However, higher sterilization doses are known to compromise mechanical properties of the device materials. Also, because corn starch is not permanently fused to the gel surface, it is easily removed by wetting, revealing the tacky gel and generating corn starch residue.
As noted above, the best gel materials tend to exhibit surfaces that are very tacky. The use of a tacky gel can make the processes of manufacturing and using gels in seals and access devices extremely difficult. A tacky gel also produces significant drag forces during instrument insertion. Furthermore, the tacky surfaces tend to draw and retain particulate matter during the manufacturing and handling processes. For these reasons it is even more desirable to render the highly tacky gel surfaces non-tacky in the case of medical devices such as access ports and other such devices.
The present invention is directed to tack-free gels and to methods for manufacturing a tack-free gel pad, comprising the steps of providing a mold; applying a fluorinated ultrahigh molecular weight polyethylene to the mold; heating a gel slurry beyond its curing temperature to a molten state, to thereby produce a molten gel; injecting the molten gel into the mold; and cooling the mold until the gel is set to thereby produce a tack-free gel.
In one embodiment, the mold is textured prior to applying the fluorinated ultrahigh molecular weight polyethylene by spraying the mold with blast media. In another embodiment, the mold is preheated to a temperature of approximately 220° F. to approximately 260° F. prior to applying the fluorinated ultrahigh molecular weight polyethylene. Alternatively, the fluorinated ultrahigh molecular weight polyethylene is applied to the mold by electrostatic coating.
In one embodiment, the fluorinated ultrahigh molecular weight polyethylene comprises a powder having a particle size of approximately 5 μm to approximately 100 μm.
In one embodiment, the mold is preheated to a temperature of approximately 110° F. to approximately 160° F. prior to injecting the molten gel.
In one embodiment, the gel slurry comprises an oil and a elastomer or elastomer. In one embodiment, the gel slurry comprises a ratio by weight of oil to elastomer of approximately 7:1 to 10:1. The oil may comprise a mineral oil and the elastomer may comprise block copolymer styrene-ethylene/butylene-styrene polymer.
In another embodiment of the method, the gel slurry is bulk degassed prior to heating the gel slurry to a molten state. In one embodiment, the gel slurry is bulk degassed at a temperature of approximately 120° F. to approximately 130° F.
An alternative method for making a tack-free gel comprises the steps of: providing a mold; applying a fluorinated ultrahigh molecular weight polyethylene to the mold; preheating the mold to a temperature of approximately 110° F. to approximately 160° F.; heating a gel slurry to a temperature of approximately 125° F.; degassing the gel slurry; dispensing the gel slurry into the mold; degassing the gel slurry a second time; and curing the gel in the mold at a temperature of approximately 140° F. to approximately 160° F. to provide a tack-free gel.
In this embodiment, the gel slurry comprises an oil and an elastomer. The oil may comprise a mineral oil and the elastomer may comprise styrene-ethylene/butylene-styrene polymer. The mold may be textured prior to applying the fluorinated ultrahigh molecular weight polyethylene by spraying the mold with blast media.
The present invention is also directed to surgical access devices adapted to provide access to a cavity in a patient while maintaining a seal between the cavity and an area outside the patient, the access device comprising a gel cap comprising a ring and a gel pad; wherein the ring is configured for alignment with an axis of an access channel defined at least in part by an incision extending through a body wall of a patient, wherein the gel pad is coupled with the ring, disposed substantially within the ring and supported at least partially thereby, the gel pad comprises a mixture of an elastomer and an oil, the gel pad comprises a self-sealing valve and defines at least a portion of an access channel, the self-sealing valve is configured to conform around an object extending through the self-sealing valve and seal the working channel in the absence of an object extending through the self-sealing valve, and wherein a discontinuous layer of polyethylene powder is permanently bonded to an outer surface of the gel pad to thereby create a tack-free surface.
In one embodiment, the polyethylene powder comprises at least one of fluorinated ultrahigh molecular weight polyethylene, unmodified ultrahigh molecular weight polyethylene, oxidized ultrahigh molecular weight polyethylene, high density polyethylene, medium density polyethylene, and low density polyethylene.
In one embodiment, the elastomer comprises at least one of polyurethane, polyvinylchloride, polyisoprene, a thermoset elastomer, a thermoplastic elastomer, a tri-block copolymer, styrene-ethylene/butylene-styrene block copolymer, styrene-isoprene-styrene, styrene-butadiene-styrene, styrene-ethylene/propylene-styrene.
In one embodiment, the oil comprises at least one of mineral oil, vegetable oil, petroleum oil, and silicone oil.
In one embodiment, the gel cap of surgical access device is configured to attach to an adjustable wound retractor.
The present invention is also directed to a method for making a tack-free gel, comprising the steps of providing a polyethylene mold; heating a gel slurry beyond its curing temperature to a molten state, to thereby produce a molten gel; dispensing the molten gel into the mold; and cooling the mold until the gel is set to thereby produce a tack-free gel.
The present invention is also directed to a method for making a tack-free gel, comprising the steps of providing a mold; spraying the mold with a polyethylene spray; heating a gel slurry beyond its curing temperature to a molten state, to thereby produce a molten gel; dispensing the molten gel into the mold; and cooling the mold until the gel is set to thereby produce a tack-free gel.
Disclosed herein is a method for producing a tack-free gel. Although described in reference to medical products, and more specifically, to gel pads for use in access systems for laparoscopic surgery, such gels may be used in a wide variety of applications, including non-medical uses, and all such applications are contemplated by this disclosure.
In
In one aspect, the elongate sleeve 56 extends through an incision to a point where an attached retention ring 58 contacts the interior portions of the body cavity and provides tension between the retainer 52 outside the body cavity and the retention ring. The retainer 52 in one aspect also supports or otherwise enables a portion of the elongate sleeve 56 to remain outside of the body cavity. Additionally, the retainer 52, retention ring 58 and elongate sleeve 56 together allow the incision to be retracted and isolated during a surgical procedure. In one aspect, the elongate sleeve 56 and aspects thereof is a wound retractor type device such as described in U.S. Pat. No. 7,650,887, the disclosure of which is hereby incorporated by reference as if set forth in full herein.
As shown, the retainer 52 and retention ring 58 are circular, but as one skilled in the art would appreciate, they may be of different shapes and sizes. The retainer 52 in one aspect may be either rigid, flexible or a combination of both. The retention ring 58 may be flexible to facilitate insertion into the body cavity. As will be described in more detail, the access device 50 includes coupling means that are adapted for coupling the cap 54 and the retainer 52 together.
A gel pad 60 may be coupled to, attached to, formed or integrated with the cap 54 so that a gas-tight conduit is formed between the cap and the sleeve 56. The gel pad 60 covers and seals the entire opening in the cap 54. In one aspect, the gel pad includes a plurality of intersecting dead-end slits 62, 64 that form an access portion or passage through the gel pad 60. Unlike foam rubber or other similar types of elastic materials, the gel pad 60 provides a gas tight seal around a variety of shapes and sizes of hands or instruments inserted therethrough.
In one aspect, the gel material from which the gel pad 60 is made is an elastomeric gel. Some such gels have been described in U.S. Pat. No. 7,473,221, U.S. Pat. No. 7,481,765, U.S. Pat. No. 7,951,076 and U.S. Pat. No. 8,105,234, the disclosures of which are hereby incorporated by reference as if set forth in full herein. The gel can be prepared by mixing a triblock copolymer with a solvent for the midblocks. The endblocks are typically thermoplastic materials such as styrene and the midblocks are thermoset elastomers such as isoprene or butadiene, e.g., Styrene-Ethylene-Butylene-Styrene (SEBS). In one aspect, the solvent used is mineral oil. Upon heating this mixture or slurry, the midblocks are dissolved into the mineral oil and a network of the insoluble endblocks forms. The resulting network has enhanced elastomeric properties over the parent copolymer. In one aspect, the triblock copolymer used is KRATON G1651, which has a styrene to rubber ratio of 33/67. Once formed, the gel is substantially permanent and, by the nature of the endblocks, processable as thermoplastic elastomers henceforward. The mixture or slurry has a minimum temperature at which it becomes a gel, i.e., the minimum gelling temperature (MGT). This temperature, in one aspect, corresponds to the glass transition temperature of the thermoplastic endblock plus a few degrees. For example, the MGT for the mixture of KRATON G1651 and mineral oil is about 120° C. When the slurry reaches the MGT and the transformation to a gel state takes place, the gel becomes more transparent, thereby providing means for visually confirming when the transformation of the slurry to the gel state is substantially complete and that the gel may be cooled. In addition to triblocks, there are also diblock versions of the materials that may be used where Styrene is present at only one end of the formula, for example, Styrene-Ethylene/Butylene (SEB).
For a given mass of slurry to form into a complete gel, the entire mass of the slurry is heated to the MGT and remains heated at the MGT for sufficient time for the end blocks to form a matrix of interconnections. The slurry will continue to form into gel at temperatures above the MGT until the slurry/gel reaches temperatures at which the components within the slurry/gel begin to decompose or oxidize. For example, when the slurry/gel is heated at temperatures above 250° C., the mineral oil in the slurry/gel will begin to be volatile and oxidize. Oxidizing may cause the gel to turn brown and become oily.
The speed at which a given volume of slurry forms a gel is dependent on the speed with which the entire mass of slurry reaches the MGT. Also, with the application of temperatures higher than the MGT, this speed is further enhanced as the end block networks distribute and form more rapidly.
The various base formulas may also be alloyed with one another to achieve a variety of intermediate properties. For example, KRATON G1701X is a 70% SEB 30% SEBS mixture with an overall Styrene to rubber ratio of 28/72. It can be appreciated that an almost infinite number of combinations, alloys, and Styrene to rubber ratios can be formulated, each capable of providing advantages to a particular embodiment of the invention. These advantages will typically include low durometer, high elongation, and good tear strength.
It is contemplated that the gel material may also include silicone, soft urethanes and even harder plastics that might provide the desired sealing qualities with the addition of a foaming agent. The silicone material may be of the types currently used for electronic encapsulation. The harder plastics may include PVC, Isoprene, KRATON neat, and other KRATON/oil mixtures. In the KRATON/oil mixture, oils such as vegetable oils, petroleum oils and silicone oils may be substituted for the mineral oil.
Any of the gel materials contemplated could be modified to achieve different properties such as enhanced lubricity, appearance, and wound protection. Additives may be incorporated directly into the gel or applied as a surface treatment. Other compounds may be added to the gel to modify its physical properties or to assist in subsequent modification of the surface by providing bonding sites or a surface charge. Additionally, oil based colorants may be added to the slurry to create gels of different colors.
The ratio of mineral oil to KRATON G1651 may be varied depending on the desired gel characteristics and the method of casting the gel pad. In one aspect, the mixture/slurry used with the various embodiments of the caps that are described herein are composed of about 90% by weight of mineral oil and about 10% by weight of KRATON G1651, a nine to one ratio. This is particularly useful in cold cast processes, as described herein. In another aspect, the mixture/slurry are composed of about 89% by weight of mineral oil and about 11% by weight of KRATON G1651, an eight to one ratio. This is preferred for use in hot cast processes, also as described herein. From a thermodynamic standpoint, these mixtures behave similar to mineral oil. Mineral oil has a considerable heat capacity and, therefore, at about 130° C. it can take 3 or 4 hours to heat a pound of the slurry sufficiently to form a homogeneous gel. Once formed, the gel can be cooled as quickly as practical with no apparent deleterious effects on the gel. This cooling, in one aspect, is accomplished with cold-water immersion. In another aspect, the gel may be air-cooled. Those familiar with the art will recognize that other cooling techniques that are well known in the art may be employed and are contemplated as within the scope of the present invention.
Many of the properties of the KRATON/oil mixture will vary with adjustments in the weight ratio of the components. In general, the greater the percentage of mineral oil the less firm the mixture; the greater the percentage of KRATON, the more firm the mixture. If the resultant gel is too soft it can lead to excessive tenting or doming of the gel cap during surgery when a patient's abdominal cavity is insufflated. Excessive tenting or doming may cause the slits 62, 64 to open, providing a leak path. Additionally, if the gel is too soft it might not provide an adequate seal. However, the gel should be sufficiently soft to be comfortable for the surgeon while simultaneously providing good sealing both in the presence of an instrument and in the absence of an instrument.
If the slurry is permitted to sit for a prolonged period of time, the copolymer, such as KRATON, and the solvent, such as mineral oil, may separate. The slurry may be mixed, such as with high shear blades, to make the slurry more homogeneous. However, mixing the slurry may introduce or add air to the slurry. To remove air from the slurry, the slurry may be degassed. In one aspect, the slurry may be degassed in a vacuum, such as within a vacuum chamber. In one aspect, the applied vacuum may be 0.79 meters (29.9 inches) of mercury, or about 1.0 atmosphere. The slurry may be stirred while the slurry is under vacuum to facilitate removal of the air. During degassing within a vacuum, the slurry typically expands, then bubbles, and then reduces in volume. The vacuum may be discontinued when the bubbling substantially ceases. Degassing the slurry in a vacuum chamber reduces the volume of the slurry by about 10%. Degassing the slurry helps reduce the potential of the finished gel to oxidize.
Degassing the slurry tends to make the resultant gel firmer. A degassed slurry composed of about 91.6% by weight of mineral oil and about 8.4% by weight of KRATON G1651, an eleven-to-one ratio, results in a gel having about the same firmness as a gel made from a slurry that is not degassed and that is composed of about 90% by weight of mineral oil and about 10% by weight of KRATON G1651, a nine-to-one ratio.
Mineral oil is of a lighter density than KRATON and the two components will separate after mixing, with the lighter mineral oil rising to the top of the container. This separation may occur when attempting to form static slurry into gel over a period of several hours. The separation can cause the resulting gel to have a higher concentration of mineral oil at the top and a lower concentration at the bottom, e.g., a non-homogeneous gel. The speed of separation is a function of the depth or head height of the slurry being heated. The mass of slurry combined with the head height, the temperature at which the gel sets and the speed with which the energy can be transferred to the gel, factor into the determination or result of homogeneous gel versus a non-homogeneous gel.
The gel pad or gel cap in various aspects of the present invention may be gamma sterilized. The relative or comparative simplicity of qualifying the sterilization process, for example of gamma versus ethylene oxide, of the gel pad and the device with the gel pad is desirable. However, under gamma sterilization large bubbles can form in the gel pad causing potential cosmetic or aesthetic issues in the sterilized devices. The bubbles are more than 99% room air, so removal of the dissolved air in the slurry is performed prior to forming the slurry into gel. For example, the slurry may be degassed via vacuum, as described above, and turned into gel by heat. Bubbles may still form in the gel during gamma sterilization but disappear in a period of about 24 to 72 hours. In one aspect, the percentage of dissolved gas in the mineral oil at room temperature is about 10%. The removal of the air in the gel has an additional effect of making the gel firmer. This however is counterbalanced by the softening effect on the gel caused by gamma radiation during gamma sterilization.
If the gel pad is to be gamma sterilized, the gel may include about 89%-90% mineral oil by weight and about 10%-11% KRATON by weight. As stated above, degassing the slurry has the effect of making the gel firmer. However, the gamma radiation softens the gel to substantially the same firmness as a gel having about 89%-90% mineral oil by weight and about 10%-11% KRATON by weight that is not degassed and gamma sterilized.
In one aspect, cyanoacrylate, e.g., SUPERGLUE or KRAZY GLUE, may be used to bond or otherwise couple or attach the gel pad 60 to the cap 54. The glue may attach to either the rubber or styrene component of the tri-block and the bond is frequently stronger than the gel material itself. In another aspect, a solvent may be used to dissolve the plastics in the cap and the polystyrene in the gel. The solution of solvent is applied to the gel pad and cap in either a spray or dip form. In effect, the solution melts both the plastic of the cap as well as the polystyrene in the gel pad to allow a chemical bond to form between the two, which remains when the solvent evaporates.
Polyethylene can be dissolved in mineral oil and then applied to the gel pad. The mineral oil will not evaporate but will over time absorb into the gel pad and impart a polyethylene layer on the gel pad that may have some beneficial properties.
In one aspect, the gel pad 60 is cast into a DYNAFLEX or KRATON polymer support structure, e.g., the cap 54. By using KRATON polymer or a similar material in the cap, ring adhesion between the gel pad 60 and the cap 54 can be achieved. The polystyrene in the gel is identified as achieving adhesion with polyphenylene oxide (PPO), polystyrene and other polymers.
The cap 54, in one aspect, includes a polymer, e.g., polyethylene (PE). In one aspect, the polyethylene is a low density polyethylene (LDPE) or high density polyethylene (HDPE), or ultrahigh molecular weight polyethylene (UHMWPE). In one aspect, the cap 54 may be made of a polymer, such as polycarbonate and may be fabricated by methods including injection molding.
The gel includes mineral oil. PE has a higher molecular weight than mineral oil. PE is dissolved by mineral oil at high temperatures. As such, as the PE and the mineral oil in the gel pad 60 intermix as both are heated to and held at temperatures above about 130° C., a bond between the PE and gel pad is formed.
In one aspect, the cap 54 includes polycarbonate. The polycarbonate of the cap 54 does not form bonds with the gel pad 60 at 130° C. However, by raising the temperature to about 150° C. for a few minutes during casting, bonding occurs between the gel pad 60 and the cap 54. As such, heating the gel pad 60 and cap 54 to temperatures at which both the polystyrene of the gel and the polycarbonate are simultaneously beyond their melt points allow bonds to form between the gel pad and the cap. Alternatively, the gel pad 60 and cap 54 may be heated to near or at the glass transition temperature of the polycarbonate cap to form the bond between the gel pad and the cap.
Referring to
Referring to
With the first and second arcs 108, 110 placed adjacent to each other, such that the first end 103 of the first arc corresponds with the second end 105 of the second arc and the second end 105 of the first arc corresponds with the first end 103 of the second arc, and prior to being snapped together, the arcs define a first, larger periphery to allow placement of a retainer 52 (
Although not shown, additional barbed portions and receiver snap engagements may be included in each arc to assist in the coupling between the cap 100 and the retainer 52 (
Referring now to
In this manner, with the latch 136 open or not engaged with the channel 140, the initial periphery of the cap 130 allows simple placement of the retainer 52 (
Referring back to
In
In one aspect, one or more of the latches 152 has notches or openings for receiving corresponding projections or protrusions extending laterally from the cap 54 to couple the retainer 150 to the cap. Additionally or alternatively, although not shown, the cap may have one or more latches hinged along the periphery of the cap for engagement with portions or edges of the retainer to releasably couple the cap and retainer together.
Referring now to
Multiple snaps 162 may be spaced along the periphery of the retainer 160. In one aspect, portions of the edge of the retainer 160 adjacent to each snap are elevated, thereby forming sidewall portions 167 on either side of each snap. The sidewall portions 167 protect the snaps 162 and strengthen or bolster the coupling between the retainer 160 and the cap 164 once coupled together. Additionally, the sidewall portions 167 facilitate handling and coupling the retainer 160 to the cap 164. Corresponding openings or cutouts 169 are disposed along the edges of the cap 164 to receive the sidewall portions 167 of the retainer 160.
Each snap 162 also has a projection 168 extending substantially perpendicular and radially inwardly from the snap. After placing or fitting a cap 164 on the retainer 160 and/or vice versa, both are squeezed together. The snaps 162 are configured to flex or deflect radially outwardly to slide over a corresponding receiver portion 170, such as a lip portion or an edge, of the cap 164 when the cap and retainer are brought together in a mating relationship. The snaps 162 are also configured to return toward a neutral position after the projection 168 on the snaps pass the receiver portion 170 of the cap 164 such that the projection of the snaps engages the receiver portion 170 of the cap. The receiver portion 170 in one aspect has an opening, aperture, notch, step, projection or other similar type of receiver or engagement means to secure the projection 168 of the snap 162 to the cap 164. Alternatively, one or more of the snaps 162 have notches or openings (not shown) for receiving corresponding projections or protrusions (not shown) extending from the cap to secure the snaps of the retainer 160 to the cap 164. The cap 164 and retainer 160 may each be made via injection molding. Additionally, the cap 164 and retainer 160 may each be made of a polycarbonate material.
In one aspect, as shown in
Referring now to
By securing the gel pad 60 to the inner cylindrical wall 172, the thickness of the gel pad and corresponding cap 54, 70, 90, 100, 130, 164, 180 is minimized along with the overall footprint of the device. A reduced thickness and overall size of the device provides a lighter device and allows for easier hand or instrument exchanges. With the gel pad thickness reduced and the gel pad being able to be substantially flush or recessed in the cap, the “doming” phenomena produced by gas pressure exerted on the body and device during insufflation is also reduced.
In various aspects (
Several of the above-described attachments could be modified to integrate the retainer or a retainer like component directly into a sleeve to which the cap is releasably coupled. Similarly, the cap may be integrated directly into the retainer and/or sleeve creating a non-releasable coupling between the components.
In one aspect, casting the gel pad 60 into the cap 54 to form a gel cap 66 includes placing the cap into a mold cavity of a casting mold. The mold cavity may include support for the annular walls of the cap 54. The mold may be made of aluminum, copper, brass, or other mold material having good heat dissipation properties. However, those familiar with the art will recognize that other mold materials having lower heat dissipation properties will produce acceptable parts and these are contemplated as within the scope of the present invention as well.
In another aspect, the gel pad 60 may be molded separately from the cap 54 and coupled to the cap 54 by a secondary operation, such as by bonding. In one aspect, the gel pad 60 may be molded into a gel slug 60 having an outer perimeter smaller than the inner cylindrical wall of the cap 54 and to a height higher that the height of the cap. The gel slug 60 may then be placed within the inner cylindrical wall of the cap 54. The gel slug 60 may be cooled and/or frozen prior to placing it within the inner cylindrical wall of the cap 54. The gel slug 60 may be coupled to the cap 54 through compression molding with the gel slug being compressed longitudinally so that the outer perimeter of the gel slug expands and compresses against the inner cylindrical wall of the cap. The gel slug 60 and cap 54 are heated to a sufficient temperature for the polystyrene of the gel and the polymer of the cap to form bonds between the gel and the cap. Molding the gel slug 60 separately from the cap 54 and heat bonding the gel slug to the cap at a later time is especially useful when the cap is made of a material that has a lower melting temperature than the MGT. In such situations, the gel slug 60 can be molded first and heat bonded to the cap 54 without melting the cap.
Whether molded with the cap or separately, when removed from the mold, the gel pad 60 typically has a tacky surface. In the present invention, the process for manufacturing the gel pad is modified to produce a permanent tack-free coating.
The process integrates powdering and casting steps into one continuous process and permanently bonds a discontinuous layer of fluorinated ultrahigh molecular weight polyethylene (UHMWPE) to the gel pad, creating a tack-free surface. The integration of powdering and casting eliminates the need for secondary powdering and cleaning processes that greatly decreases the amount of time required to touch up gel pads and clean the molds. Using previous processes for manufacturing gel pads, gel remnants are removed from the gel pad, which is then powdered and cleaned of excess oil and powder. The molds of gel that are cast at room temperature and cured in an oven, are left with a sticky residue and require considerable amounts of clean up. Using this new process, the gel is cast hot from an injection molding machine or from an extruder and is free of remnants. Excess powder on the gel pad can be quickly removed using a wipe. Also, pre-powdered molds have no residue and the excess powder left behind in the mold can easily be removed.
The use of polyethylene powder as opposed to starch powder also contributes to process and product improvement. Polyethylene significantly lowers the bioburden of the gel pad as polyethylene is not a growth medium for microorganisms. Further, during the new hot casting process the polyethylene powder is essentially fused onto the surface of the gel, thus eliminating the chance of losing coating residue during gel pad use. In addition, the new process creates a discontinuous coating that doesn't interfere with any of the functional properties of the product or mechanical properties of the material such as sealing and elasticity, respectively. The discontinuous coating allows the gel to be stretched and return to its original form without surface cracking occurring. A continuous coating must have similar elasticity as the gel to prevent cracking or delamination. Materials with high elasticity are generally tacky, the conforming nature of elastomers make it unlikely to have a tack-free surface.
Preferably, gel molds are textured prior to being used in the manufacturing process. Texturing helps stabilize particles on the gel surface by inhibiting particle flow, which would result in uneven particle placement. An abrasive blast cabinet may be utilized to texture the molds. Molds, for example, aluminum molds, are placed inside the cabinet and sprayed with blast media (grit range from about 80 to about 100 grit/mesh) using a pneumatically powered hose until the surface of the mold is uniformly textured. The molds are then removed and sprayed with an air hose to remove excess media.
As an alternative to texturing the molds, the molds may be preheated to a temperature of approximately 240° F. so that the particles adhere more strongly to the smooth surface of the mold. In still another embodiment, charged particles can be held in place during casting by the process of electrostatic coating (e-coating). The electrically conductive molds attract and hold charged particles that are applied to the surface by either spraying or dipping the mold. The e-coating process is robust enough to hold the particles in place until the molten gel is dispensed into the mold.
The molds are powdered with fluorinated UHMWPE prior to adding the gel. In one embodiment, the fluorinated UHMWPE is a powder. In one embodiment, the particle size of the fluorinated UHMWPE powder is approximately 40-50 μm. In another embodiment, the particle size of the fluorinated UHMWPE powder is approximately 45 μm. The particle size of the fluorinated UHMWPE can be varied depending on the desired degree of tackiness. In general, very small particles pack more densely, providing a more tack-free surface, particularly when the underlying gel is stretched.
In other embodiments, other powders than fluorinated UHMWPE can be used to achieve a tack-free surface. Assorted forms of polyethylene powder can be used similarly to the fluorinated UHMWPE. Oxidized UHMWPE essentially provides identical results to that of the fluorinated UHMWPE, the only difference being the method utilized for surface modification of the powder. Also, oxidized UHMWPE may leave a slight residue on the hand after handling gels post radiation sterilization. Other forms of polyethylene powder, such as high density polyethylene (HDPE), medium density polyethylene (MDPE), low density polyethylene (LDPE), and unmodified UHMWPE, can also be employed to achieve the desired tack-free product. However, different powders and their respective particle size provide variable coverage of the tack-free layer. In general, particle sizes ranging from 24 μm to 350 μm may be used to provide gels of varying degrees of tackiness.
In some embodiments, the fluorinated UHMWPE powdered mold is preheated prior to adding the molten gel. Optionally, the powdered mold is preheated with a cap ring or other insert, depending on the final gel product. In one embodiment, the mold is preheated to a temperature range of approximately 110-160° F. The skilled artisan will appreciate that the preheating temperature may vary depending on the thickness of the mold walls and that molds made from very thin walls may not require preheating.
A gel slurry comprising an oil and an elastomer or co-polymer is heated beyond its curing temperature to a molten state and added to the powdered mold. In some embodiments, the oil comprises at least one of mineral oil, vegetable oil, petroleum oil, and silicone oil. In one embodiment, the oil is a mineral oil.
In some embodiments, the elastomer comprises at least one of polyurethane, polyvinylchloride, polyisoprene, a thermoset elastomer, a thermoplastic elastomer, a tri-block copolymer, styrene-ethylene/butylene-styrene block copolymer, styrene-isoprene-styrene, styrene-butadiene-styrene, styrene-ethylene/propylene-styrene. In one embodiment, the elastomer is a block copolymer styrene-ethylene/butylene-styrene polymer. In another embodiment, the elastomer is KRATON G1651.
The ratio by weight of oil to elastomer may vary depending on the desired consistency of the final gel product. For products such as a gel cap useful as an access device in surgery, gel slurries having a ratio by weight of oil to elastomer from approximately 7:1 to approximately 10:1 are useful. In one embodiment, the ratio by weight of oil to elastomer is 8:1.
Because the higher temperatures used to heat the gel slurry to a molten state result in a reduction in molecular weight via oxidative degradation, resulting in a softer durometer gel, a lower ratio of oil to elastomer is generally used than in a cold cast process to compensate for the loss in firmness. By way of example, if a gel is normally produced using a 9:1 ratio by weight of mineral oil to elastomer in a cold-cast process, an 8:1 ratio by weight of mineral oil to elastomer would be used to produce a gel product of similar firmness using the present hot-cast method. As one skilled in the art will appreciate, other ratios may be used to achieve the desired gel characteristics.
In one embodiment, the gel slurry is bulk degassed and pumped into an injection molding machine or an extruder, where it is heated beyond its curing temperature to a molten state. The gel slurry may be degassed at room temperature or at higher temperatures. In one embodiment, the gel slurry is degassed at approximately 125° F.
The molten gel, in one embodiment having a temperature of approximately 460° F. to approximately 480° F., is cast into the mold. If the mold contains a cap or other insert, the gel is cast such that the gel is in contact with the cap/insert.
The powdered mold lid is placed and the unit is cooled to room temperature. The gel cap 66 may be cooled, such as by air-cooling, cold-water immersion, or other cooling means that are well known in the art. At 150° C. the gel pad is soft and if it were distorted during cooling it would set with the distortion included. To reduce the likelihood of distorting the gel pad 60, the gel cap 66 may be cooled within the mold. Cooling times may vary based on parameters including size and configuration of the mold, quantity of gel, temperature and quantity of cooling medium, cooling medium properties and the mold material. As an example, the cooling time may be about two (2) hours if cooling in air and about fifteen (15) minutes if cooling in water. Whether cooling with air or water, the final properties of the gel are substantially the same. The gel cap 66 is typically cooled to about ambient room temperature, but may be cooled to lower temperatures.
The gel cap 66 may be removed from the mold at any time after the gel has set. The powdered molds facilitate demolding as the powder acts as a mold release agent. Accordingly, the gel pad may be removed simply by inverting the mold. The molds are then cleaned and prepared to repeat the process. Using the hot cast process described above, the molten gel is dispensed into the mold as a homogeneous mixture with minimal free oil, eliminating the waxy residue left by cold cast processes after demolding and producing molds that are easier to clean and a consistent tack-free surface on the gel pad. This is significant, because gel slurry batches can vary in the amount of free oil present in the slurry and can lead to difficulties in achieving consistent results. Using a molten gel eliminates this problem.
An overview of the process for producing gel pads having a discontinuous permanent tack-free coating is shown in
Although the preferred process for producing a tack-free gel involves hot casting molten gel, the process can also be used in cold-casting gels. In a cold-cast process, the gel slurry is generally used at a 9:1 ratio by weight of oil to co-polymer. The slurry is heated to approximately 125° F. during degassing before dispensing the degassed slurry into molds, optionally with a cap ring, and degassed a second time prior to curing the gel in the molds at approximately 150° C. for approximately 1.5 hours. The molds can be pre-powdered with fluorinated UHMWPE to provide a tack-free gel, as described above, but because there is more free mineral oil present in the gel slurry, a waxy residue is left behind on the molds after demolding that requires additional cleaning steps before the molds can be reused. Also, gel slurries are more heterogeneous than a molten gel and thus produce a less consistent tack free surface.
In an alternative embodiment of the described methods for producing a tack-free gel, polyethylene molds having varying densities (LDPE, HDPE, for example) can be used in place of traditional metallic molds. In this process, no pre-powdering is required. Gel is cast into the polyethylene mold and cooled to room temperature. Once cool, the gel can be peeled from the mold, with a thin layer of polyethylene transferring to the gel, producing a tack-free surface. Gel can be cast using the above mentioned mold injection method or using a “hot pot” type method. In the “hot pot” method, gel is heated and stirred until molten and poured into a desired cavity. This method may be difficult to control, however, and the molded in stress from the plastic molds sometimes leads to cracks and defects on the tack-free surface. In addition, the high temperatures required to make the gel molten can cause the polyethylene molds to melt or deform and the gel to degrade. As an alternative to the polyethylene mold, a polyethylene insert in a metal mold may be used. The insert is an injection molded polyethylene dish shaped like the desired gel product, which is placed into the mold prior to adding the molten gel. The mold supports the insert and gel. Once the gel is cool, it can be removed from the mold and the insert, leaving a thin layer of polyethylene deposited on the surface of the gel.
Another embodiment utilizes an aerosol polyethylene spray. As with the polyethylene mold process, this method does not require pre-powdering. In this embodiment, molds are sprayed with a polyethylene spray, leaving a thin layer of polyethylene on the surface of the mold. Gel is hot cast into the sprayed molds and cooled to produce a gel product having a residue of polyethylene, leaving behind a tack-free surface. The gel may be cast by either mold injection or the “hot pot” technique. However, it can be difficult to get a uniform coating of polyethylene by spraying the mold surface, producing an uneven distribution of polyethylene on the gel product surface after demolding. A light coating will leave sections of the gel tacky and a heavy coating will lead to cracking of the tack-free layer. Additionally, aerosol sprays release volatile organic compounds (VOCs) to the environment and so are not preferred for manufacturing processes.
Accordingly, the present invention provides a gel having a permanent tack-free coating, methods for making a gel with a permanent tack-free coating and use of such gel in access devices. Although this invention has been described in certain specific embodiments, many additional modifications and variations would be apparent to those skilled in the art. It is therefore to be understood that this invention may be practiced otherwise than specifically described, including various changes in the size, shape and materials, without departing from the scope and spirit of the present invention. Thus, embodiments of the present invention should be considered in all respects as illustrative and not restrictive.
This application claims the benefit of U.S. Application No. 62/026,317, filed Jul. 18, 2014, the entire disclosure of which is incorporated by reference.
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WO 0108563 | Feb 2001 | WO |
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WO 2005009257 | Feb 2005 | WO |
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WO 2005034766 | Apr 2005 | WO |
WO 2005089661 | Sep 2005 | WO |
WO 2006040748 | Apr 2006 | WO |
WO 2006059318 | Jun 2006 | WO |
WO 2006100658 | Sep 2006 | WO |
WO 2007044849 | Apr 2007 | WO |
WO 2008015566 | Feb 2008 | WO |
WO 2008093313 | Aug 2008 | WO |
WO 2008121294 | Oct 2008 | WO |
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Entry |
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Number | Date | Country | |
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20160015425 A1 | Jan 2016 | US |
Number | Date | Country | |
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62026317 | Jul 2014 | US |