COMPONENT FOR CONVEYING GASES
20220379054 · 2022-12-01
Inventors
Cpc classification
B29L2023/007
PERFORMING OPERATIONS; TRANSPORTING
F16L11/111
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
A61M2205/0233
HUMAN NECESSITIES
B29C48/09
PERFORMING OPERATIONS; TRANSPORTING
B29C48/13
PERFORMING OPERATIONS; TRANSPORTING
F16L53/38
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B29C48/303
PERFORMING OPERATIONS; TRANSPORTING
A61M16/00
HUMAN NECESSITIES
B29C48/32
PERFORMING OPERATIONS; TRANSPORTING
A61M2207/00
HUMAN NECESSITIES
International classification
Abstract
This invention provides for a component forming a part of a breathing tube, or forming the breathing tube, for example as a part of a breathing circuit for respiratory therapy. The component comprising a tubular body having a foamed wall. The foamed wall can be formed from extrusion of a single extrudate. The foamed wall is of a sufficient minimum optical transparency such that, in use, there is enabled the visual detection of a liquid (or condensate that may have formed) within the tubular body.
Claims
1-81. (canceled)
82. A component forming a part of a breathing tube, or forming the breathing tube, comprising: a tubular body having a foamed wall formed from a single extrudate, and wherein the foamed wall is surface modified by altering the surface energy of the wall surface.
83. The component of claim 82, wherein said altering the surface energy of the wall surface comprises increasing the surface energy of the wall surface.
84. The component of claim 82, wherein the foamed wall is surface modified by chemical means or physical means.
85. The component of claim 82, wherein the wall of the tubular body is corrugated, or of a corrugate profile, wherein the corrugation profile comprises alternating outer crests or annular protrusions and inner troughs or annular recesses.
86. The component of claim 82, wherein the wall thickness is about 0.4 mm to about 0.8 mm.
87. The component of claim 82, wherein the foamed wall is thermally insulative of, at least, the interior of the tubular body bounded by the foamed wall.
88. The component of claim 82, wherein the foamed wall has a thermal conductivity of about 0.2 to 0.4 W/(m.Math.K) (Watts per meter degrees Kelvin).
89. The component of claim 82, wherein the foamed wall has a void fraction of up to about 10%, or wherein the foamed wall has a void fraction of about 5.5% to about 7.5%.
90. The component of claim 82, wherein the extrudate comprises one or more polymer(s).
91. The component of claim 82, wherein the extrudate comprises one or more of Linear Low Density Polyethylene (LLDPE), Low Density Polyethylene (LDPE), Polypropylene (PP), Polyolefin Plastomer (POP), Ethylene Vinyl Acetate (EVA), plasticised Polyvinyl chloride (PVC), or blends of these materials.
92. The component of claim 82, wherein the extrudate further comprises one or more chemical foaming agents.
93. The component of claim 82, wherein the extrudate further comprises one or more surface modification agents.
94. The component of claim 82, wherein the extrudate further comprises one or more surface modification agents comprising glycerol monostearate (GMS), ethoxylated amine, alkanesulphonate sodium salt, or lauric diethanolamide.
95. The component of claim 82, wherein the extrudate comprises a polymer or polymers being at least about 98.4 weight percent (wt. %) of the total extrudate.
96. The component of claim 82, wherein the extrudate comprises a chemical foaming agent as at least about 0.005 weight percent (wt. %) of the total extrudate.
97. The component of claim 82, wherein the extrudate comprises a surface modification agent as at least about 0.05 weight percent (wt. %) of the total extrudate.
98. The component of claim 82, wherein the resultant formed tubular body enables surface property contact angles of less than about 45 degrees (°).
99. The component of claim 82, further comprising a heater.
100. The component of claim 99, wherein a heater is associated with a wall of the tubular body.
101. The component of claim 82, wherein the tubular body further comprises an outer sheath.
102. The component of claim 101, wherein the outer sheath traps air between adjacent outer crests or annular protrusions and restrains a heater, such as a heater wire, associated with an exterior wall surface of the tubular body.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0119] Preferred embodiments of the invention will be described by way of example only and with reference to the drawings, in which:
[0120]
[0121]
[0122]
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[0124]
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[0127]
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
[0128] In the field of medical circuits, and in particular breathing circuits (including anaesthetic circuits), condensation or rain-out can be a particular problem where high humidity breathing gases come into contact with the walls of a component at a relatively lower temperature. Enhancing the thermal resistance (or thermal insulation capabilities) of the walls provides benefits in this respect. However, it remains beneficial for a user or care-giver to be able to optically identify or visually discern the presence of liquid or build-up of condensate within the component. The present invention is directed toward enabling a component providing a patient and care-giver with both of these beneficial requirements.
[0129] With reference to
[0130] In response to the user set humidity or temperature value input via dial 110, for example, and other inputs, the controller determines when (or to what level) to energise heater plate 107 to heat the water 106 within humidification chamber 105. As the volume of water within humidification chamber 105 is heated, water vapour begins to fill the volume of the chamber above the water's surface and is passed out of the humidification chamber outlet 104 with the flow of gases (for example air) provided from a gases supply means or ventilator/blower 115 which enters the chamber 105 through inlet 116. Exhaled gases from the patient's mouth are returned to the ventilator via a return expiratory breathing tube 130.
[0131] The ventilator 115 is provided with variable pressure regulating means or variable speed fan 121 which draws air or other gases through blower inlet 117. The speed of variable speed fan 121 is controlled by electronic controller 118. It will be appreciated that the patient interface 102 could equally be a nasal mask, oral mask, oronasal mask, nasal prongs or full-face mask, etc.
[0132] However, there are also other competing requirements that should be satisfied by medical tubing in the field of the present invention. For example, it is preferable that breathing tubes for breathing circuits are: resistant to crushing; resistant to restrictions in flow when bent (increased resistance to flow<50% when bent around a 1 inch cylinder); resistant to kinking; resistant to changes in length/volume under internal pressure (compliance); resistant to leaking (<25 ml/min@6kPa); have low flow resistance (increase in pressure@max. rated flow<0.2 kPa); electrically safe i.e.: sparks in the tubing can be extremely dangerous, especially in oxygen-rich environments such as oxygen therapy.
[0133] International standard ISO 5367:2000(E) (Fourth edition, 2000 Jun. 1) is one example of how some of these desirable parameters are measured and assessed, and the document is hereby incorporated into this specification in its entirety by reference. It is preferable that components of the invention meet or exceed some or all of these standards.
[0134] In this specification, terms “medical circuit” and “breathing circuit” are used to indicate the general field of the invention. It is to be understood that a “circuit” is intended to include open circuits, which do not form a complete closed circuit. For example, CPAP systems usually consist of a single inspiratory breathing tube between a blower and a patient interface. The term “breathing circuit” is intended to include such “open circuits”. Similarly, the term “medical circuit” is intended to include both breathing circuits and insufflation circuits (which are also typically “open”). Similarly, the term “medical tubing” is intended to be read as flexible tubing suitable for use in the type of medical circuits described above connecting between components of a medical circuit and providing a gases pathway between components of a medical circuit.
[0135] The term “substantially uniform” wall thickness corrugated tube is intended to mean a tube having a corrugation profile wherein an outer peak, for example, comprises the maximum outside radius of the tube while also forming the maximum inner radius of the tube and an inner trough, for example, forms the minimum inner and outer radius of the tube. This type of tube is typically formed from a substantially uniform thickness extrusion that is subsequently corrugated. It will be appreciated that the subsequently formed corrugations may vary the wall thickness of the outer peak regions versus the inner trough regions of the finished tube. The ratio of minimum to maximum actual wall thickness may vary as much as 1:1.5-3.0 for example.
[0136] It will be generally understood that a “single extrudate” as used in this specification and claims means a single batch, or blend, or formulation, or mixture of material (or materials), that is fed to an extruder to be extruded. In this manner, a single layer extrusion is formed. It will be appreciated that this is in contrast to a multi-layer extrudate, such as for example those formed by co-extrusion or extrusion-coating techniques.
[0137] The phrase “visual detection” as used in this specification and claims is intended to mean recognition by human eye, for example, a person is able to visually recognise the presence, or build-up of a liquid (or condensate that may have formed) within at least a part of the tubular body. A further example includes where people are capable of visually recognising the presence or build-up of a liquid (or condensate that may have formed) in a tubular body according to this invention, when subjected to the “visual detection test method” as described herein.
Breathing Tubing
[0138] Medical tubing in the field of the present invention has a nominal bore size from approximately 10 mm to approximately 30 mm, and lengths ranging from approximately 300 mm to 2.5 m. In particular applications such as medical tubing to connect to an interface component the tubing may be significantly shorter (e.g. 50 mm to 300 mm). A catheter mount for example, may have a length of approximately 80 mm. A catheter mount is a single lumen tube which in use will carry both inspiratory and expiratory breathing gases to and from a patient respectively.
Foamed Embodiment
[0139] In a first embodiment there is provided a component 1 forming a part of a breathing tube (such as for example inspiratory tube 103), or forming the breathing tube. The component 1 comprises of a tubular body 2 having a foamed wall 3 formed from extrusion of a single extrudate. The foamed wall 3 is of a sufficient minimum optical transparency such that, in use, enables visual detection of a liquid (or condensate that may have formed) within the tubular body 2.
[0140] In another embodiment however, there is provided a component 1 forming a part of a breathing tube (such as for example inspiratory tube 103), or forming the breathing tube. The component 1 comprises of a tubular body 2 having a foamed wall 3 formed from extrusion of a single extrudate. Alternatively in another embodiment, there is provided a component 1 forming a part of a breathing tube (such as for example inspiratory tube 103), or forming the breathing tube. The component 1 comprises of a tubular body 2 having a foamed wall 3, the tubular body 2 formed from a single extrudate, where the tubular body further comprises of an outer sheath 7. In both these embodiments, additional features and combinations with such embodiments are contemplated in the form of, for example, optional heating elements, external sheaths, techniques for surface modification of the tubular body's wall, including ways and amount of foaming of the wall 3, and whether the conduit is of a corrugated form or not.
[0141] In yet further embodiments however, there is provided a component 1 forming a part of a breathing tube (such as for example inspiratory tube 103), or forming the breathing tube. The component 1 can comprise of a tubular body 2 having a wall 3 with a modified surface, the tubular body formed from a single extrudate. Alternatively, in another embodiment, there is provided a component 1 forming a part of a breathing tube (such as for example inspiratory tube 103), or forming the breathing tube. The component 1 can comprises of a tubular body 2 having a wall 3 with a modified surface, the tubular body 2 formed from a single extrudate, where the tubular body further comprising of an outer sheath 7. Again, and as stated previously, in both these embodiments additional features and combinations with such embodiments are contemplated in the form of, for example, optional heating elements, external sheaths, techniques for surface modification of the tubular body's wall, including ways and amount of foaming of the wall 3, and whether the conduit is of a corrugated form or not.
[0142]
[0143]
[0144] In contrast, although not specific to the illustration of
[0145] The wall 3 of such a tubular body 2 can be optionally corrugated, or of a corrugate profile (for example as shown in
[0146] The tubular body 2 advantageously has a substantially uniform wall thickness. A wall thickness of about 0.2 mm to about 1 mm, or about 0.3 mm to about 0.9 mm, or about 0.4 mm to about 0.8 mm, or about 0.5 mm to about 0.7 mm, or about 0.3 mm to about 0.6 mm, or about 0.4 mm to about 0.7 mm. The wall may be about 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9 or 1 mm thick.
[0147] Such a foamed wall 3 preferably provides a level of thermal insulative of, at least, the interior (or gas flow passage) of the tubular body 2 bounded by the foamed wall 3. In particular, the wall 3 is thermally insulative of the contents (such as for example humidified gases flowing through the gas flow passage) of the tubular body 2 to the potential cooling effects of the environment surrounding the tubular body (for example, insulating from the ambient air surrounding a breathing circuit, or a laparoscopic insufflation system). The environment surrounding the component or tubular body 2 is for example, a hospital ward or room, an operating theatre, or other locations where the patient may be located.
[0148] The foamed wall 3 is a single-piece of a foamed polymer material, for example being formed by extrusion of a single extrudate.
[0149] Foaming of the tubular body's wall 3 allows enhanced thermal insulative properties of the component as part of a breathing tube or breathing circuit, for example. More specifically, the foamed wall 3 may provide for overall increased thermal insulative properties of the component, particularly of, at least, the interior of the tubular body bounded by the foamed wall. In various embodiments the foamed wall 3 has or provides for a thermal conductivity of about 0.2 to about 0.4 W/m-° K (Watt per meter Kelvin). It will however be appreciated the foamed wall 3 may beneficially provide for other levels of thermal conductivity, advantageously thermal conductivities of about 0.15 to 0.35 W/m-° K or of about 0.25 to 0.45 W/m-° K are preferred.
[0150] As part of foaming the wall of the tubular body 2, the foaming provides for certain gas voids 18 within the wall 3. A quantitative measure of the gas voids 18 can be expressed as a void fraction. A void fraction is indicative of the volume of void (gas) space occupying a unit volume of the tubular body.
[0151] The gas voids 18 may assist in contributing to the insulation performance of the component 1, in addition to enabling the desired level of tubular wall transparency.
[0152] A minimum level of transparency of the tubular wall 2 enables the visual detection of liquid (or condensate that may have built-up within the tubular body or component) by a person.
[0153] Various levels of void fraction can be of up to about 10%, or up to about 9%, or up to about 8%, or up to about 7%, or up to about 6% or up to about 5%, or up to about 4%, or up to about 3%, or up to about 2%, or up to about 1%, or ranges of void fractions of the tubular body's wall of about 1%, of about 1.5%, of about 2%, of about 2.5%, of about 3%, of about 3.5%, of about 4%, or about 4.5%, or about 5%, or about 5.5%, or about 6%, or about 6.5%, or about 7%, or about 7.5%, or about 8%, or about 8.5%, or about 9%, or about 9.5%, or about 10%.
[0154] According to the applicant's test results, the most preferred void fractions to be formed in a tubular body's wall is about 5.5% or about 7.5%, or is about 5.5% to about 7.5%. Such void fractions enable a person to optically identify or visually discern the presence of liquid, accumulated liquid or other build-up of condensate (for example as a result of rain-out).
[0155] The tubular body's foamed wall 3 can be foamed either by physical foaming techniques, or by chemical foaming techniques, or by a combination of both of these.
[0156] The extrudate may comprise of a number of polymer materials to which other materials may be added (for example by blending as or to form a master batch). Preferred materials include one or more polymer(s) of Linear Low Density Polyethylene (LLDPE), Low Density Polyethylene (LDPE), Polypropylene (PP), Polyolefin Plastomer (POP), Ethylene Vinyl Acetate (EVA) or blends of these materials.
[0157] Plasticised PVC may also be a suitable material, but it is not as well accepted for environmental reasons.
[0158] The polymer material can comprises at least about 98.4, 98.5, 98.6, 98.7, 98.8, 98.9, 99.0, 99.1, 99.2, 99.3, 99.4, 99.5, 99.6, 99.7, 99.8, or 99.9 weight percent (wt. %) of the total extrudate. In particular embodiments the polymer material comprises about 99.49 wt. % of the total extrudate (as LLDPE).
[0159] Alternatively preferably the polymer comprises about 99.488 wt. % of the total extrudate.
Surface Modification
[0160] One such additional material that can be included with the extrudate is one or more surface modification agents.
[0161] A surface modification agent may preferably comprise glycerol monostearate (GMS), ethoxylated amine, alkanesulphonate sodium salt, or lauric diethanolamide.
[0162] Preferably the surface modification agent comprises at least about 0.05, 0.1, 0.15, 0.2, 0.25, 0.3, 0.35, 0.4, 0.45, 0.5, 1.1, 1.2, 1.3, 1.4, or 1.5 weight percent (wt. %) of the total extrudate. More preferably the surface modification agent comprises about 0.25 wt. % of the total extrudate. Alternatively preferably the surface modification agent comprises about 0.5 wt. % of the total extrudate.
[0163] For example, MLDNA-418 supplied by Clariant (New Zealand) Ltd. and under the product name “418 LD Masterbatch Antistatic” is a surface modification agent master batch with 5(±0.25)% glycerol monostearate (CAS No. 123-94-4) as an active ingredient.
[0164] A surface modification agent may additionally be included in the extrudate. Such an agent assists in increasing the surface energy (or the wettability) of the surface of the formed component or tube. In this manner, advantageously increasing the surface energy may act to promote reduced contact angles between drops or beads of condensate or liquid that may build up on the surface.
[0165] The contact angle is the angle formed by the solid surface of the component or tube wall and the tangent line to the upper surface at the end point of a liquid droplet. Contact angle measurement is a non-destructive method of determining the wetting behaviour of liquids on a solid surface. It enables the calculation of surface and interfacial tension along with spreading coefficients. The surface tension calculated from the contact angle data are a characteristic measurement for the respective surface and fluid system.
[0166] The contact angle between a liquid and a surface is measured using a goniometer (angle measurement device). A precise volume of the liquid is dispensed on the cleaned and dried flat test surface using a precision syringe. The droplet is allowed to stabilize for a few seconds and a high magnification camera is used to capture the image of the droplet. The image is digitised and the angle between the test surface and the tangent line along the droplet surface is measured.
[0167] Reducing contact angle increases contact area between the droplet and solid surface, and also reduces droplet thickness, enhancing heat conduction through the droplet. Both effects increase droplet evaporation rate.
[0168] Increasing the energy of a surface reduces contact angle of a droplet placed on the surface. In this manner, a droplet of liquid on the surface of a higher energy surface can preferentially have a greater surface area in contact with the surface, then a surface of relatively lower energy.
[0169] Advantageously, the droplet may be spread across a larger surface area of the surface and, therefore, be more likely to re-evaporate into the gas stream flowing through the component or tube.
[0170] For example, the droplet or bead may spread across the internal surface of the tube's wall, allowing greater surface area for re-evaporation into the passing gas stream.
[0171] In another example, where the tube is corrugated (whether as an annular corrugate or spiral corrugate form), the droplet or bead of water is more likely to form in a part of the corrugation of low temperature position (i.e. generally this is a part of the corrugation closest to or most exposed to ambient conditions surrounding the tube). In such a case, altering the surface properties of the tube surface can promote a droplet or bead formed at the low temperature position to spread across the tube surface and in doing so may move towards a region of warmer temperature. Such migration of movement of the droplet or bead can allow for further improved re-evaporation rates, both due to the droplet possibly moving toward regions of warmer temperatures, as well as possibly toward regions of the tube which are exposed to greater or faster gas stream flows. Greater re-evaporation rates may therefore be achieved by providing for improved migration of a droplet or bead radially inward from the internal surface wall of the tube.
[0172] In respect of surface modification, it should be appreciated that in various aspects of the invention, a component 1 and its tubular body 2 can be formed from a single extrudate where the body 2 has a modified surface. Modified surfaces may preferably facilitate the advantages of re-evaporation rates or droplet migration as described above.
[0173] Some of the other methods which may be used to increase surface energy include: [0174] Physical [0175] Physical adsorption [0176] Langmuir-Blodgett film [0177] Chemical [0178] Oxidation by strong acids [0179] Ozone treatment [0180] Chemisorption [0181] Flame treatment [0182] Radiation [0183] Plasma (glow discharge) [0184] Corona discharge [0185] Photo-activation (UV) [0186] Laser [0187] Ion beam [0188] Electron beam [0189] γ-irradiation
[0190] A chemical additive or agent can also be used to impart the increase in surface energy and wettability to the component or tube so formed.
[0191] Such a surface modification agent may for example be glycerol monostearate, a food grade emulsifier.
TABLE-US-00001 TABLE 1 Contact angle measurements for samples of LLDPE with different surface treatments Average Contact Angle Description of Surface Liquid (degrees) Linear Low-density Polyethylene (LLDPE), Water 97.39 as manufactured Linear Low-density Polyethylene (LLDPE), Water 67.56 fluorinated, washed Linear Low-density Polyethylene (LLDPE), Water 44.98 plasma-treated, 10% O2, 300 Watts, 30 seconds Linear Low-density Polyethylene (LLDPE), Water 33.09 with 5% MLDNA-418 as surface modification agent additive
[0192] The sample with 5% MLDNA-418 surface modification agent produced the lowest measured contact angle compared to other surface modification methods tested.
[0193] In Table 1 above and where referenced elsewhere in this specification, contact angle measurements were based on static drop shape testing methods conducted in accordance with ASTM Standard D7334, 2008, “Standard Practice for Surface Wettability of Coatings, Substrates and Pigments by Advancing Contact Angle Measurement”.
[0194] Modifying the surface properties of the tubular body 2 (i.e. the foamed wall 3 of the resultant tubular body) enables variation of the surface property contact angles.
[0195] By choosing various surface modification methods, it is possible to provide a foamed wall 3 having surface property contact angles of less than about 50, 45, 40, 35, 30, 25, 20 degrees (°), as measurable by an angle measurement device such as a geniometer.
[0196] Advantageously, foamed walls 3 of a resultant tubular body enabling surface property contact angles of less than about 35° appear to provide useful results.
Foaming
[0197] Another additional material to be included with the extrudate is one or more chemical foaming agents.
[0198] A chemical foaming agent enables foaming of the extrudate material as part or after the extrusion process.
[0199] For example, the chemical foaming agent can comprise at least about 0.005, 0.006, 0.007, 0.008, 0.009, 0.01, 0.011, 0.012, 0.013, 0.014, 0.015, 0.016, 0.017, 0.018, 0.019, or 0.02 weight percent (wt. %) of the total extrudate.
[0200] In preferred embodiments, the chemical foaming agent can comprise about 0.01 wt. % to about 0.012 wt. % of the total extrudate.
[0201] As part of a chemical foaming extrusion process, the polymer resin component of an extrudate is mixed with a chemical foaming agent. Chemical foaming agents are sometimes also referred to as blowing agents.
[0202] Some preferred chemical foaming agents include those that comprise calcium oxide. For example, MHYNA-CF20E supplied by Clariant (New Zealand) Ltd. under the product name Hydrocerol CF20E is a chemical foaming agent in the form of a blowing agent master batch with about 0.5-1% calcium oxide as an active ingredient.
[0203] During a chemical foam extrusion process the polymer resin component and chemical foaming agent(s) are mixed and melted. The chemical foaming agent(s) decomposes and liberates gas which is dispersed in the polymer (or master batch or extrudate) melt and which expands upon exiting the die of an extruder.
[0204] It will also be appreciated other foaming techniques can be employed for the forming of a foamed wall 3 of the component 1 or tube, such as by physical rather than chemical foaming methods. Physical foaming methods would include gas being introduced directly into the melt or extrudate while under pressure. As the melt or extrudate is then extruded the pressure is reduced allowing the gas to expand. For example, one such physical foaming technique includes blowing or injecting of gas(es) into extrudate at or near the point of extrusion. Such gas(es) may include nitrogen, carbon dioxide, pentane or butane.
Heaters and Sheaths
[0205] The component 1 can optionally further include a heater 6 (as shown for example in
[0206] The heater can be associated with a wall of the tubular body, for example an interior wall surface (such as
[0207] In other embodiments, the heater can be embedded, either partially or wholly, in the wall 3 of the tubular body 2 (not shown).
[0208] In yet a further embodiment, the tubular body 2 can optionally include an outer sheath 7. Such an outer sheath 7 surrounds the tubular body 2.
[0209] Where a heater is associated with an exterior surface of the tubular body 2, the sheath 7 would additionally surround or envelope the heater.
[0210] However, it is also contemplated that in various aspects of the invention an outer sheath 7 may surround the component 1, whether a heater is included with the tubular body 2 or not.
[0211] The sheath 7 is contemplated as being provided in various forms. For example, the sheath 7 may be applied about the tubular body 2 as an extruded outer layer, as a wrapping about the body 2, or as a sleeve that is slid or pulled into position about the tubular body 2. Such a sheath 7 may be formed of similar materials as the tubular body 2, for example LLDPE (low low density polyethylene). The sheath 7 may assist in further improving thermal performance of the tubular body 2. The sheath 7 may be of any necessary thickness, although thickness and the material used should be balanced with the need to maintain flexibility of the tubular body 2.
[0212] In one embodiment it is contemplated an outer sheath 7 may have a wall thickness of about 100 micrometres.
[0213] Where an outer sheath 7 is extruded about the tubular body 2, for example, such an extrusion could be a sequential step to initial extrusion of the tubular body 2, that is, an extrusion step post-formation of the body 2. Further, where an outer sheath 7, for example, is a wrap about the body 2, the sheath 7 may be of a tape or ribbon form and can be spirally wound about the length of the body 2. Still further, where an outer sheath 7 is pre-formed as a hollow tube, it may be sleeved into position about the outside of the body 2.
[0214] Where a heater 6 is employed however, the heater 6 can be of a heater wire form. Materials for such heater wires are copper, aluminium or a PTC (positive temperature coefficient) type material. Aluminium is not as conductive as copper, but may be an economical choice even though the wire diameter is larger for the same resistance. While the applied circuit voltage is intrinsically safe (less than 50V), for corrosion resistance and best electrical safety in the event of the tube or sheath being damaged, the wire will ideally be self insulated, either by enamel coating or anodising in the case of aluminium. Alternatively an extruded plastic sheath can be fitted about the heater wire.
[0215] Further advantageously, the outer sheath 7 may trap air between adjacent outer crests 4 (or annular protrusions). This may assist in further insulation of the gas passing through passage of the component 1. Where for example a heater 6 is employed with the component 1 and an outer sheath is also used, the outer sheath 7 can help to restrain the heater 6, such as a heater wire, in position when the heater is associated with an exterior wall surface of the tubular body.
[0216] Where the component 1 is a breathing tube, or a part of a breathing tube, it can be terminated by a first connector 8 at an inlet 9 and a second connector 10 at an outlet 11 (for example as shown in
[0217] In other contemplated forms, the component 1 with its tubular body 2 can form a part or further component of a conduit for use in at least part of an insufflation system (for example such as that shown in
Foamed Heater Embodiment
[0218] In another embodiment there is provided a component 1 forming a part of a breathing tube, or forming the breathing tube (such as for example as illustrated in
[0219] The foamed wall 3 is of a sufficient minimum optical transparency that, in use, enables visual detection of a liquid (or condensate that may have formed) within the tubular body 2.
[0220] The details for such a further embodiment are similar to that previously described in the first embodiment above.
[0221] Reference can also be made to
[0222]
[0223] More particularly, with this embodiment the heater 6 is associated with a foamed wall 3 of the tubular body 2.
[0224] It will be appreciated there are various forms in which the heater 6 can be associated with a wall of the tubular body as previously discussed.
[0225] In a further option, the tubular body 2 may optionally be surrounded by an outer sheath 7, the operation and benefits of which are previously discussed. The outer sheath 7 may be employed, whether or not a heater 6 is also included.
[0226] In both the embodiments described above, such a method of forming a component 1 forming a part of a breathing tube, or forming the breathing tube, comprises extruding a tubular body from a single extrudate. The single extrudate including a foaming agent for foaming of the tubular body so formed, such that, the wall 3 of the foamed tubular body 2 is of a sufficient minimum optical transparency that is use enables visual detection of a liquid (or condensate that may have formed) within the tubular body 2.
[0227] In one such embodiment, the method comprises passing the formed extruded tubular body 2 into a corrugator and forming corrugations along the extruded tubular body having a corrugation profile comprising alternating outer crests 4 (or annular protrusions) and inner troughs 5 (or annular recesses). The corrugator may form annular or spiral corrugations.
[0228] In one embodiment of the invention, the component forming a part of a breathing tube, or forming a breathing tube, is formed according to the steps of i) mixing or providing of a master batch of extrudate material (i.e. material for extrusion), ii) feeding the master batch to an extrusion die head, iii) extruding the extrudate into a tubular body for the component. Optionally, the tubular body is further fed into a corrugator for forming of corrugations.
[0229] Such a master batch can be provided with a chemical foaming agent included, and optionally a chemical surface modification agent may be included (although it will be appreciated other forms of surface modification agent techniques may be used, for example the physical techniques as described herein).
[0230] In one example, the process used to make such a component involves extruding a molten tubular profile into a corrugator machine utilising an endless chain of mould blocks to form a flexible corrugated tube.
[0231] An extruder such as a Welex extruder equipped with a 30-40 mm diameter screw and typically a 12-16 mm annular die head with gap of 0.5-1.0 mm has been found to be suitable for producing low cost tubes quickly. Similar extrusion machines are provided by American Kuhne (Germany), AXON AB Plastics Machinery (Sweden), AMUT (Italy), Battenfeld (Germany and China).
[0232] A corrugator such as those manufactured and supplied by Unicor® (Hassfurt, Germany) has been found to be suitable for the corrugation step. Similar machines are provided by OLMAS (Carate Brianza, Italy), Qingdao HUASU Machinery Fabricate Co., Ltd (Qingdao Jiaozhou City, P.R. China), or Top Industry (Chengdu) Co., Ltd. (Chengdu, P.R. of China).
[0233]
[0234] During manufacture, the molten tube 16 is passed between a series of rotating moulds/blocks on the corrugator after exiting the extruder die head 15 and is formed into a corrugated tube such as that illustrated in
[0235] The molten tube is formed by vacuum applied to the outside of the tube via slots and channels through the blocks and/or pressure applied internally to the tube via an air channel through the centre of the extruder die core pin. If internal pressure is applied, a specially shaped long internal rod extending from the die core pin and fitting closely with the inside of the corrugations may be required to prevent air pressure escaping endways along the tube.
[0236] The tube 1 has a wall 3 that is preferably between approximately 0.3-1 mm thick for a breathing tube of typical dimensions (i.e. between approximately 10 mm and 30 mm diameter for neonatal and adult applications respectively and approximately 1-2 meters in length).
[0237] Such a component according to this invention may also include includes a plain cuff region for connection to an end connector fitting.
[0238] Similarly, the end connector fitting of the present tube is preferably of a standard type (moulded plastic) according to the intended use of the medical tubing and may preferably be permanently fixed and/or air tight by friction fit, adhesive bonding, over moulding, or by thermal or ultrasonic welding etc. For example, the end connector may incorporate an internal medical taper.
[0239] One advantage of the preferred type of component or tube manufacture described above with reference to
[0240] Manufacture speeds can be significantly increased by the reduction in complexity and elimination of secondary manufacturing processes. While this method is an improvement over separate cuff forming processes, a disadvantage of the prior art plain cuff is that the corrugator must slow down to allow the wall thickness of the tube in this area to increase (the extruder continues at the same speed).
[0241] The cuff thickness is increased to achieve added hoop strength and sealing properties with the cuff adaptor fitting.
[0242] Further, the heat of the molten polymer in this thicker region is difficult to remove during the limited contact time with the corrugator blocks and this can become an important limiting factor on the maximum running speed of the tube production line.
Condensate Accumulation Test—Performance Results
Test Method
[0243] The test circuit is laid horizontally inside a wind or convection tunnel. Air flow inside the tunnel is set to about 0.5 m/s and the room ambient temperature is maintained at about 18° C. which is at the lower-end recommended use temperature for the humidifier. The tube is connected to a humidification chamber that delivers moisture-saturated (i.e. >95% RH) air at 37° C.
[0244] Condensate is allowed to accumulate inside the tube and the weight gained by the tube in 16 hours is recorded as the accumulated condensate.
Condensate Test Experimental Results
[0245]
TABLE-US-00002 TABLE 2 Condensate accumulation in breathing tube samples with different additive concentrations Condensate Reduction Accumulation versus in 16 hours current Sample Description (grams) product (%) Current product 127.18 — Linear Low-density Polyethylene (LLDPE) Linear Low-density Polyethylene (LLDPE) 115.98 9 With 5% MLDNA-418 Surface Modification Agent Linear Low-density Polyethylene (LLDPE) 105.34 17 With 10% MLDNA-418 Surface Modification Agent Linear Low-density Polyethylene (LLDPE) 118.11 7 With 1.0% CF20E Foaming Agent Linear Low-density Polyethylene (LLDPE) 114.93 10 With 1.2% CF20E Foaming Agent Linear Low-density Polyethylene (LLDPE) 90.1 29 With 5% MLDNA-418 Surface Modification Agent and 1.0% CF20E Foaming Agent Linear Low-density Polyethylene (LLDPE) 83.16 35 With 5% MLDNA-418 Surface Modification Agent and 1.2% CF20E Foaming Agent
[0246] Trends indicate that increasing surface modification agent content increases the impact of surface modification in condensate accumulation inside the tube. Results indicate that the benefit from foaming and surface modification in reducing condensate is more than a linear accumulation. It appears there are synergistic benefits from the combination of foaming agent with a surface modification agent. Foaming agents produce air bubbles inside the tube during extrusion. Air has a very low thermal conductivity which causes a significant increase in the thermal insulation property of the tube.
[0247] From these results, it is apparent that small variations in the composition of the mix will have a significant impact to performance.
Visual Detection Test Method
[0248] Six (6) polyethylene breathing tube samples (corrugated, 22 mm diameter and 1.5 meter long) having MHYNA-CF20E foaming agent concentrations of 0%, 1%, 1.2%, 1.5% and 1.8%, and 2.0% were assembled using standard breathing circuit heater wires and connectors. A precision syringe was used to inject 100 mL of clean deionized water in each of the tubes. Air was allowed to pass through the test breathing tubes from a portable ventilator.
[0249] The tubes with 0% (current state-of-the-art) and 2% MHYNA-CF20E (foaming agent master batch) were used as references to represent the extreme ends of the transparency range to be evaluated, where for example, 0% having an acceptable water detectability (Reference A) and 2% MHYNA-CF20E having no water detectability at all (Reference B).
[0250] Ten (10) volunteer participants with varying age, ethnicity and gender were asked to conduct a visual inspection of the tubes and evaluate the ease with which they detected water inside the tube compared to the reference tubes in a scale of 1 to 5, as per the following guideline: [0251] Water detectability is as good as in Reference A [0252] Water is detectable but not as good as in Reference A [0253] Water is reasonably detectable [0254] Water is barely detectable but not as bad as Reference B [0255] Water is as undetectable as in Reference B
[0256] Nine (9) out of ten (10) participants rated the tube with 1.2% MHYNA-CF20E as having reasonable water detectability with an average score of 3. On the other hand, the tube with 1% MHYNA-CF20E scored an average of 2. 10 out of 10 participants considered the tube as having reasonable or better water detectability than the rest of the test samples except Reference A. Results of the study showed that the 1.5% and 1.8% MHYNA-CF20E (greater than 10% foam/void fraction) have unacceptable amount of foaming with 10 out of 10 indicating that the two tubes have very poor water detectability.
Further Performance Results
[0257] Table 3 sets out comparative data between reference samples of 100% LLDPE corrugate tubes (see reference samples 1, 2, 3) against corrugated tubes of similar dimensions formed with a polymer material of LLDPE plus other materials. Reference sample 1 is the current state-of-the art having a 100% LLDPE corrugate tube and an internal coiled heater. Reference sample 2 is a 100% LLDPE tube with an internal coiled heater and outer sheath of polyethylene. Reference sample 3 has a 100% LLDPE tube with an external filament heater and outer polyethylene sheath.
[0258] As shown, the various comparative corrugate tube forms comprises LLDPE as a polymers material plus a chemical foaming agent (examples 1, 2, 3), LLDPE plus a chemical surface modification agent (examples 4, 5, 6, 7), and LLDPE plus a combination of a chemical foaming agent and a chemical surface modification agent (examples 9, 10, 11, 12).
[0259] The examples exemplify the performance of the various tubes in respect of their condensate accumulation test results (test procedure being the same as the data obtained in Table 2). Notably, the results for examples 9-12 provide significant improvement over the reference samples in terms of reduction in accumulated condensation.
[0260] The examples also exemplify the surface modification achieved by including a chemical surface modification agent within the extrudate. Notably, the surface property contact angle (for water) was altered from about 97° in the reference samples to about 33° in the examples using a surface modification agent.
[0261] Further, there are unexpected improvements in the condensate accumulation test results for examples 9-12. The foaming of the wall and alteration of surface properties of the wall surface provide for improved condensate accumulation results over the reference samples. Those improvements are not a linearly cumulative of the benefits that appear provided by either foaming or surface modification on their own. Such non-linear accumulation of performance indicates the synergistic benefits of such combination.
[0262] It is believed the particular improvements are resultant from the combination of increased void fraction in the tube wall (i.e. about 5.5% to 7.5% void fraction) due to foaming (and therefore thermal resistance to heat losses from warm gases passing through the tube), and possibly enhanced re-evaporation rates of condensate or other liquid build-up in the tube due to reduced surface property contact angle for liquid on the wall surface within the tube.
[0263] Addition of an outer sheath to an extruded 100% LLDPE tube reduced condensate accumulation by 26.7%. Furthermore, external filament heating of a 100% LLDPE tube reduced condensate accumulation by 53.1%. Externally heating a surface modified tube that has not been foamed did not give any condensate reduction benefits. On the other hand, externally heating a foamed conduit (without surface modification) gave about a further 4.6% condensate reduction.
[0264] However, external filament heating of a foamed and surface-modified breathing tube gave a 27.8% less condensate compared to a similarly externally heated 100% LLDPE tube. This further demonstrates the synergistic benefit from the combination of foaming and surface-modification in minimizing condensate accumulation inside a humidified breathing circuit.
TABLE-US-00003 Surface Surface Base Foaming modification Void Tube wall Property material (X agent (wt. agent (wt. Wall fraction thermal Contact Tube wt. % of % of total % of total thickness of tube conductivity Angle examples extrudate) extrudate) extrudate) (mm) (%) (W/m ° K) (degrees) Reference 100% (0%) (0%) Crest- 0 0.4 97 sample 1 LLDPE 0.3 Trough- 0.6 Reference 100% (0%) (0%) Crest- 0 0.4 97 sample 2 LLDPE 0.3 Trough- 0.6 Reference 100% (0%) (0%) Crest- 0 0.4 97 sample 3 LLDPE 0.3 Trough- 0.6 Example 99.99% Calcium (0%) Crest- 5.5 0.3 97 1 LLDPE oxide 0.4 (0.01%) Trough- 0.7 Example 99.988% Calcium (0%) Crest- 7.5 0.3 97 2 LLDPE oxide 0.5 (0.012%) Trough- 0.7 Example 99.988% Calcium (0%) Crest- 7.5 0.3 97 3 LLDPE oxide 0.5 (0.012%) Trough- 0.7 Example 99.5% (0%) Glycerol Crest- 0 0.3 33 4 LLDPE monostearate 0.3 (0.25%) Trough- 0.6 Example 99.0% (0%) Glycerol Crest- 0 0.3 30 5 LLDPE monostearate 0.3 (0.5%) Trough- 0.6 Example 99.5% (0%) Glycerol Crest- 0 0.3 33 6 LLDPE monostearate 0.3 (0.25%) Trough- 0.6 Example 99.5% (0%) Glycerol Crest- 0 0.3 33 7 LLDPE monostearate 0.3 (0.25%) Trough- 0.6 Example 99.0% 0%) Glycerol Crest- 0 0.3 33 8 LLDPE monostearate 0.3 (0.5%) Trough- 0.6 Example 99.49% Calcium Glycerol Crest- 5.5 0.3 33 9 LLDPE oxide monostearate 0.4 (0.01%) (0.25%) Trough- Example 99.488% Calcium Glycerol Crest- 7.5 0.3 33 10 LLDPE oxide monostearate 0.5 (0.012%) (0.25%) Trough- 0.7 Example 99.49% Calcium Glycerol Crest- 5.5 0.3 33 11 LLDPE oxide monostearate 0.4 (0.01%) (0.25%) Trough- 0.7 Example 99.488% Calcium Glycerol Crest- 7.5 0.3 33 12 LLDPE oxide monostearate 0.5 (0.012%) (0.25%) Trough- 0.7 Heater wire used (yes/no, Improvement location e.g. Average over within tube, Condensate existing Improvement Improvement outside tube, Outer accumulation product, over over embedded sheath Tube over 16 hrs reference reference reference in wall used examples (grams) sample 1 sample 2 sample 3 of tube) (yes/no) Reference 127.18 NA NA NA Internal No sample 1 Coiled Heater Reference 93.17 26.7% NA NA Internal Yes sample 2 Coiled Heater Reference 59.59 53.1% 36.0% NA External Yes sample 3 Filament Heater Example 118.11 7.1% −26.8% −98.2% Internal No 1 Coiled Heater Example 114.93 9.6% −23.4% −92.9% Internal No 2 Coiled Heater Example 56.85 55.3% 39.0% 4.6% External Yes 3 Filament Heater Example 115.98 8.8% −24.5% −94.6 Internal No 4 Coiled Heater Example 105.34 17.2% −13.1% −76.8% Internal No 5 Coiled Heater Example 81.45 36.0% 12.6% −36.7% Internal Yes 6 Coiled Heater Example 61.82 51.4% 33.6% −3.7% External Yes 7 Filament Heater Example 61.43 51.7% 34.1% −3.1% External Yes 8 Filament Heater Example 90.10 29.2% 3.3% −51.2% Internal No 9 Coiled Heater Example 83.16 34.6% 10.7% −39.6% Internal No 10 Coiled Heater Example 70.36 44.7% 24.5% −18.1% Internal Yes 11 Coiled Heater Example 43.05 66.2% 53.8% 27.8% External Yes 12 Filament Heater
Component of an Insufflation System
[0265] Laparoscopic surgery, also called minimally invasive surgery (MIS), or keyhole surgery, is a modern surgical technique in which operations in the abdomen are performed through small incisions (usually 0.5-1.5 cm) as compared to larger incisions needed in traditional surgical procedures. Laparoscopic surgery includes operations within the abdominal or pelvic cavities.
[0266] In abdominal surgery, for example, the abdomen is usually insufflated with carbon dioxide gas to create a working and viewing space. The gas used is generally CO2 which is common to the human body and can be absorbed by tissue and removed by the respiratory system. It is also non-flammable, which is important because electrosurgical devices are commonly used in laparoscopic procedures. The use of these devices tends to create surgical smoke in the working space due to burning of tissue. Smoke evacuation systems which use a discharge arm or limb are commonly used to remove the smoke from the surgical site, so that a surgeon can see what he or she is doing, and so that this potentially harmful material does not remain within the body cavity post-surgery.
[0267] A typical smoke evacuation system generally includes a trocar and a cannula at the end to aid insertion into the operative site. The smoke exits the insufflated abdominal area through the discharge limb. The discharge limb may be attached to the end of a laparoscopic instrument so as to provide evacuation close to the site where electrocautery takes place. Usually, the gases and smoke from the body cavity are filtered through a filter to remove particulate matter before they are vented to atmosphere.
[0268] It has been common practice in laparoscopic surgery to use dry gases. However, it is also desirable for the CO2 or other insufflation gas to be humidified before they are passed into the abdominal cavity. This can help prevent ‘drying out’ of the patient's internal organs, and can decrease the amount of time needed for recovery from surgery.
[0269]
[0270] The smoke evacuation system 202 comprises a discharge or exhaust limb 205, a discharge assembly 207 and a filter 206. The discharge limb 205 connects between the filter 206 and the discharge assembly 207, which in use is located in or adjacent to the operative site. The discharge limb 205 is a self-supporting conduit or tube (the conduit is capable of supporting its own weight without collapsing) with two open ends: an operative site end and an outlet end is made of a breathable foamed material as described in this specification.
[0271] When saturated gases pass out of the abdominal cavity, they contact the cooler walls of the discharge limb, which is normally around one metre in length or thereabouts and moisture in the gases tends to condense onto the walls of the discharge limb or exhaust conduit. Water vapour can also condense on the filter, which can saturate the filter and cause it to become blocked. This potentially causes an increase in back pressure and hinders the ability of the system to clear smoke.
[0272] The present medical tubing as described above with reference to breathing tubes is also suitable for application in the delivery limb of a surgical humidification system. In particular, the medical tubing of the present invention is appropriate for use in the evacuation or exhaust limb of a smoke evacuation system. The performance benefits of the tubing are a result of the improved rainout performance (i.e. less condensation forming) of the tubes of the present invention.
Other Applications
[0273] It is anticipated that the present invention will find other medical applications to which it is particularly suited. For example, applications where consistent heating or maintenance of heating of tubing conveying a humid gas in order to reduce the formation of condensation could benefit from the low cost and efficient heating of the present invention.
[0274] The foregoing description of the invention includes preferred forms thereof. Modifications may be made thereto without departing from the scope of the invention
[0275] To those skilled in the art to which the invention relates, many changes in construction and widely differing embodiments and applications of the invention will suggest themselves without departing from the scope of the invention as defined in the appended preliminary claims. The disclosures and the descriptions herein are purely illustrative and are not intended to be in any sense limiting.