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Butylene

Butylene is a four-carbon alkene with the chemical formula C4H8.
It is an important industrial chemical used in the production of fuels, lubricants, and various petrochemicals.
Butylene can exist in multiple isomeric forms, including 1-butene, 2-butene, and isobutene, each with unique properties and applications.
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Most cited protocols related to «Butylene»

Cyclic butylene terephthalate oligomers [CBT100, Mw = (220)n g/mol, n = 2–7, melting point = 130 ÷ 160 °C] and butyltin chloride dihydroxide catalyst (96%, melting point 150 °C) were purchased from IQ-Holding Distributor of products previously commercialized by Cyclics Europe GmbH ((Schwarzheide, Germany) and Sigma-Aldrich (currently Merck Life Science S.r.l., Milano, Italy), respectively. Acetone (99+%) was purchased from Alfa Aesar (Thermo Fisher (Kandel) GmbH, Kandel, Germany).
Different types of GRM were selected for the present study, among materials with relatively large commercial availability and focusing on low surface oxidation. Selection was neither aimed to be comprehensive nor to represent all the different production methods and producers, but was exclusively carried out to cover a wide span GRM structural features, including lateral size, surface area and defectiveness. The main structural features of the selected GRM are summarized in Table 1. It is worth mentioning that, independently on the terminology used by the producers of the commercial products addressed here, all the different grades are considered to be graphite nanoplates, accordingly with terminology proposed by Bianco et al. [35 (link)] and will be referred in this work to as GRM-#, as assigned in Table 1. All the materials were used as received. Furthermore, GRM−4 and GRM-5 were selected to undergo annealing for 1 h at 1700 °C at ~50 Pa in a vacuum oven (Pro.Ba., Cambiano, Italy) to decrease the structural defectiveness, as previously reported [58 (link)]. High-temperature annealed material are referred to as GRM-4T and GRM-5T.
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Publication 2020
Acetone butylene Chlorides Fever Graphite terephthalate Vacuum
To develop the target material, a polymer substrate was selected, sensor sensitivity to magnetic material concentration and material thickness were tested and optimum values selected, and then material properties, sensitivity, error from applied compression, and durability of the new material were characterized.
We sought to develop a ferrous target made up of a polymer substrate seeded with iron powder. The basis for using iron powder is that it was demonstrated effective previously in development of a ferrous sheath [22 (link)]. The sensing element, which may be placed either on or within the wall of the prosthetic socket [19 (link),21 (link)], is a coil antenna of diameter 32.0 mm and thickness 0.15 mm made using flexible circuit technology [13 (link)]. A surface-mounted capacitor is affixed to the antenna. This sensing element is wired to an inductive sensing chip (LDC1614, Texas Instruments, Dallas, TX, USA) so that when it is powered the inductor and capacitor operate as an LC tank oscillator. The magnetically permeable target near the sensor reinforces the inductor and lowers the sensor’s oscillation frequency in a distance-dependent manner. Therefore, changes in sensor frequency measured by the inductive sensing chip are a sensitive measure of the distance between the antenna and the magnetically permeable target. The sensor is calibrated in the socket using spacers of known thickness [14 (link)].
Outside of woven forms, most thermoplastics are not flexible or elastic enough to match the properties of prosthetic liners and thus serve as the polymer substrate. Three potential exceptions are thermoplastic vulcanizates (TPV), thermoplastic polyurethanes (TPU), and thermoplastic elastomers (TPE). TPVs are fully cross-linked ethylene propylene diene terpolymer (EPDM)/polyolefin phase (PP) compounds. TPUs are thermoplastic elastomers consisting of linear segmented block copolymers composed of hard and soft segments. TPEs are copolymers that can be a mixture of polymers. They have both thermoplastic and elastomeric properties. These polymers mimic the mechanical behavior of elastomers while retaining the ability to be heated and molded. TPEs encompass a much broader range of elasticities than the others; TPVs and TPUs fall at the stiff end of the TPE tensile elasticity spectrum. Samples of both TPV and TPU polymers were tested to see if their properties could be modified sufficiently to achieve the range of desired liner elasticity. Preliminary test results showed that at the highest plasticizer loading possible, which would create the lowest stiffness material, samples from both TPV and TPU groups remained beyond the high end of the stiffness range of most elastomeric liners (tensile stiffness >309 kPa) [23 (link)]. Thus, TPV and TPU materials were not considered further, and TPEs were selected for development in the present study.
Three TPEs were considered. The first material, 4044, is a SEEPS (styrene–ethylene–ethylene/propylene–styrene) polymer. The second material, 2063, is a SPS (styrene–propylene–styrene) polymer. The third material, an alloy, is made from two different SBS (styrene–butylene–styrene) polymers. The styrene content of each polymer and the average molecular weight of the chains are the most influential factors that determine polymer strength. Different midblock chemistries affect the amount of plasticizer the polymer can absorb and thus its elasticity, but of equal importance a variety of chemistries provide a good chance of finding a suitable adhesive for bonding the target to the elastomer or fabric backing of a typical prosthetic liner product. Preliminary testing demonstrated 4044 the most promising of these three polymers in that it demonstrated compressive and tensile elasticities within the desired range for this application.
Ferrous target samples of thickness ranging from 0.50 to 1.00 mm were fabricated for testing. To make the samples, light mineral oil was mixed with Septon 4044 (Kurarary America, Pasadena, TX, USA), placed on a hotplate, and stirred until it congealed. Iron powder was added, the material mixed, and then placed into the base of a mold (coated with a release agent) that had venting channels (Figure 2). Three molds were used, of heights 0.50, 0.75, and 1.00 mm. A top plate was loaded with weights to compress the viscous polymer so that excess polymer was forced out through the venting channels. The mold was allowed to cool, and the material was removed and cut into 50.8 mm diameter samples for testing.
A high iron concentration compared with a low iron concentration will induce a stronger signal from the inductive sensor but will increase cost and may also increase the tensile elasticity of the target. In prior efforts developing a polyurethane-based target within a prosthetic sheath fabric, we found that a concentration of 75% to 83% produced an appropriate sensitivity [22 (link)]. In the present study using the TPE polymer, three iron concentrations were evaluated (75%, 77%, and 85% by weight). It was expected that the highest concentration (85%) would approach saturation of the signal, thus experience minimal error from compressive stress compared with the lower concentrations.
To characterize sensitivity of the inductive sensor to targets of different iron concentration, a testing jig was used (Figure 3). The jig allowed the inductive sensor antenna to be positioned above a target sample at a known height, recorded using a height gauge (570–312, Mitutoyo, Aurora, IL, USA) with resolution of 0.01 mm. The antenna was adjusted in incremental steps, 0.25 mm for distances up to 2.00 mm, and 1.00 mm for distances between 2.00 mm and 15.00 mm.
A thinner magnetic target is preferable since it occupies less volume in the socket and is thus less disruptive to prosthesis users. Thicknesses of 0.50, 0.75, and 1.00 mm were tested.
To characterize sensitivity of the inductive sensor to target thickness, the testing jig shown in Figure 3 was used. Data points were concentrated at low distance so as to obtain an accurate sensitivity reading in the high sensitivity region of the calibration curve and to ensure the 0.00 mm distance was well defined. The antenna was adjusted in incremental steps, 0.05 mm for distances up to 0.60 mm, 0.25 mm for distances between 0.60 mm and 2.00 mm, and 1.00 mm for distances above 2.00 mm but less than 15.00 mm.
Compression testing was conducted using procedures similar to those described previously for testing prosthetic liners [23 (link)]. A material testing machine was used (Instron 5944, Norwood, MA, USA). Samples were of dimension 19.0 mm diameter. Synthetic lubricant (Outlast, C & C Synthetics, Mandeville, LA, USA) was applied to the target material samples to reduce friction. Samples were cyclically preconditioned for 15 minutes from 0 to 250 kPa at a rate of 100% strain per second and then re-lubricated before the test. They were then compressed to 60% strain at a rate of 150% strain per second. Tests were conducted until two cycles of repeatable stress strain response were achieved.
Measured engineering stress was converted to true stress under the assumption of material incompressibility. Compressive elasticity (CE) was calculated as the tangent modulus between 10% and 40% strain [23 (link)]. Three samples were tested, and the overall CE was the arithmetic mean of the three of them.
Tensile testing was conducted using procedures similar to those described previously for testing prosthetic liners [23 (link)]. Samples of target material of dimension 170.0 mm × 31.3 mm were adhered at the ends of a custom test fixture equipped with linear slide rails to accommodate the changing thickness in the sample during the test. The two halves of the jig were installed using parallel blocks to ensure the sample was properly aligned. The sample was pulled at a displacement rate of 30 mm/s until a 60% strain was achieved. The sample was allowed to rest for 20 minutes and then the test was rerun. Testing was repeated until two consistent results were achieved.
Engineering stress was converted to true stress using the assumption of incompressibility. From the resulting stress strain plot, the slope of the tangent line to the curve between strains of 10% and 40% was calculated. The slope of this line was the tensile elasticity for each sample. Three samples were tested, and the overall tensile elasticity was the arithmetic mean of the three of them.
Volumetric elasticity testing was conducted similar to that described previously for liner testing [23 (link)]. Samples 10.0 mm in diameter and 1.0 mm thick were coated with synthetic lubricant and placed in a 10.0 mm diameter well. Six samples were stacked in the well to achieve a thickness comparable to prosthetic liners tested previously (approximately 6.0 mm). The plunger of the tensile testing machine was lowered into the well and compressed the specimen at 0.1 percent strain per second up to 500 kPa compression. Tests were conducted until two cycles of repeatable stress strain response were achieved. Using the highest loads tested, the line tangent to the linear region was calculated and the slope reported as the volumetric elasticity (VE).
Using the VE and CE values for each sample, we calculated the Poisson ratio using Hooke’s law and the definition of Poisson ratio: PR=3VECE6VE
Evaluations were conducted to characterize sensor sensitivity to compressive stress. A base with a cutout space was used to isolate the antenna and keep it at a consistent distance from the target (2.0 mm) during testing (Figure 4). A 1.6 mm-thick plate of quartz glass (elasticity of 72 GPa) was placed on top of the base to minimize deformation of the support jig. Testing machine load and displacement data (Instron 5944, Norwood, MA, USA) were collected simultaneously with sensor data.
A 50.8 mm diameter target material sample was centered above the antenna. Preliminary testing demonstrated that samples tended to stick to the platen during testing, thus a thin layer of synthetic lubricant was applied to the sample. Six pre-conditioning cycles from 10 kPa to 425 kPa were applied. The crosshead rate was 30 mm/s during loading and unloading. A pressure of 425 kPa was held for 15 s during each cycle. Addition of the lubricant introduced a “toe” region to the material property curve at pressures below 25 kPa. Lubricant was squeezed out from between the platen and test sample. Therefore, after preconditioning, the pressure was stepped from 25 kPa to 425 kPa in 40 kPa increments and held for 15 s at each pressure.
Durability testing was conducted using a fabric–polymer–fabric stack-up so that the 0.50 mm-thick polymer target did not fold over itself when the test sample was worn in the shoe of an able-bodied person. The stack-up was made in a two-step process. First, a 0.50 mm-thick sample of the ferrous polymer was overlaid onto a 0.60 mm-thick sheet of nylon spandex (FLNS, Seattle Fabrics, Inc., Seattle, WA, USA). This construct was placed in a mold and heated to mechanically bond together. This process was repeated on the opposite surface with a second layer of fabric so as to sandwich the 0.50 mm-thick ferrous polymer sample between the two fabric sheets. Samples of 50.8 mm diameter were punched out of the finished stack-up. These samples were affixed to the silicone elastomer from a prosthetic liner using silicone adhesive (Sil-Poxy, Smooth-On, Inc., Macungie, PA, USA). The elastomer from the liner was 63.5 mm in diameter and 2.30 mm in thickness (Figure 5).
One testing sample was worn in each shoe under the metatarsal region of the foot by a 65.7 kg male for 14 days. A smart phone step counter was used to monitor the number of steps during the test period. Over 14 days, the mean step count was 2,123 steps/day. Calibration tests were performed before the sample was worn (pre-wear) and were repeated at 1d, 3d, 7d, 10d and 14d of wear. The elastomeric liner material affixed to the sample plastically compressed over time, which was accounted for in calibration by shifting the zero position of the sample by the reduced thickness.
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Publication 2019
The synthesis was carried out using two different melting stages with different levels of vacuum (Figure 1). It was conducted by dosing calculated amounts of materials based on 1 mole of dicarboxylic acid. The first melting stage was the esterification stage, the second was the polycondensation stage. The esterification progressed at approximately 200–210 °C. The theoretical amount of by-products was obtained through esterification against dimethyl terephthalate and 1,4-butanediol with the 0.75 (g/mole) TBT catalyst and sebacic acid was added to the second esterification reaction against oligomer (T-B). The esterification was finished after obtaining the theoretical amount of calculated by-products. After esterification, we initiated polycondensation by increasing the temperature to 240 °C and decreasing the vacuum level (1.5 torr). All experiments were conducted using different molar ratios of sebacic acid and dimethyl terephthalate; the ratio of 1,4-butanediol to dicarboxylic acid was fixed as 1.25:1 mol/mol.
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Publication 2020
Anabolism Butylene Glycols Dicarboxylic Acids dimethyl 4-phthalate Esterification Molar sebacic acid Vacuum
Thermal properties of PLA and PLA/PBSA blends were investigated by calorimetric analysis (Q200 TA- DSC). Nitrogen, set at 50 mL/min, was used as purge gas for all measurements. Indium was used as a standard for temperature and enthalpy calibration of DSC. The materials used for DSC analysis have been cut from the ISO 5271-A dog-bone injection mold specimens. In order to evaluate if an eventual crystallization occurred during the specimen injection molding (affecting the mechanical behavior of the materials), the thermal properties were evaluated considering only the first DSC heating run. The sampling was carried out taking the material in the same region of the specimens to avoid differences ascribable to different cooling rates in the specimen thickness. The samples, with mass between 11.5 and 15 mg, were sealed inside aluminum pans before measurement. PBS granules were also analyzed in order to better understand how its thermal properties could affect the thermograms of the binary blends.
The samples were quickly cooled from room temperature to −50 °C and kept at this temperature for 1 min. Then the samples were heated at 10 °C/min to 200 °C to delete the thermal history then a second cooling scan from −70 °C to 190 °C, at 10 °C/min, was carried out. Melting temperature (Tm) and cold crystallization temperature (Tcc) of the blends were recorded at the maximum of the melting peak and at the minimum of the cold crystallization peak, respectively. The enthalpies of melting and cold crystallization were determined from the corresponding peak areas in the thermograms. Where possible the PLA and PBSA crystallinity were calculated according the following Equation: Xcc, PLA(or PBSA) =ΔHm, PLA (or PBSA) ΔHcc, PLA (or PBSA) ΔH°m, PLA (or PBSA) · wt. % PLA (or PBSA)
where Xcc, is the crystallinity fraction of PLA or PBSA, ΔHm and ΔHcc are the melting and cold crystallization enthalpies respectively, while Δm is the theoretical melting heat of 100% crystalline polymer. For PLA a Δm value of 93 J/g [71 (link)] and for PBSA a Δm value of 142 J/g were considered [8 (link)].
The heat deflection temperature or heat distortion temperature (HDT) corresponds to the temperature at which the polymeric material deforms under a specified load. This property is fundamental during the design and production of thermoplastic components. The HDT is also strictly correlated to the polymer crystallinity, in fact it is noteworthy that a highly crystalline polymer has an HDT value higher than its amorphous counterpart [72 (link)]. For this purpose, the determination of the deflection temperature under load (HDT) was carried out on a CEAST HV 3 (INSTRON, Canton, MA, USA) in accordance with ISO 75 (method A). A flexural stress of 1.81 MPa and a bath heating rate of 120 °C/h were used. The sample size was 80 mm × 10 mm × 4 mm. When the sample bar deflects by 0.34 mm, the corresponding bath temperature represents the HDT (Type A) value. At least five measurements were carried out and the average value was reported.
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Publication 2021
Aluminum Bath Bones Calorimetry Cold Temperature Crystallization Cytoplasmic Granules Indium Nitrogen poly(tetramethylene succinate-co-tetramethylene adipate) Polymers Radionuclide Imaging Thermography
hBM-MSCs were isolated and cultured as previously described [17 (link),21 (link),42 (link),43 (link)]. Briefly, hBM-MSCs were isolated from the waste samples from surgery consisting of bone marrow extracted throughout washouts of the femurs’ medullary cavities of adult donor subjects undergoing primary total hip replacement. The procedure of isolation of stem cells is occasional and is not part of a specific project. All procedures were done after the consent of donors (60-year-old) and were in accordance with the Declaration of Helsinki.
Donor subjects gave informed consent and the institutional ethical committee approved the procedures. After density gradient on Lympholyte (Cedarlane Laboratories Limited, Hornby, ON, Canada), mononuclear cells were isolated from the bone marrow and were seeded in culture flasks in growth medium consisting of RPMI-1640 (Euroclone, Milano, Italy) medium containing FBS 10%, 2 mM L-glutamine, and 1% penicillin–streptomycin (Euroclone) in a humidified atmosphere and 5% CO2 at 37 °C. After 5 to 7 days, the non-adherent cells were removed, and fresh medium was added to the flasks. After 15 days, a fibroblast-like colony started to grow. The medium was changed every three days [17 (link),21 (link),42 (link),43 (link)]. The mesenchymal phenotype of hBM-MSCs was analyzed by flow cytometry FACScan (BD Biosciences, San Jose, CA, USA ) as previously described [21 (link)]. The human anti-CD44, -CD45, -CD73, -CD90, -CD105, human leukocyte antigen (HLA)-ABC (BD Biosciences) were used. Data analyses were performed with the FlowJo software (Tree Star, Ashland, OR, USA). Cells were electronically gated according to light-scattering properties to discriminate cell debris. Isotype-matched nonspecific antibodies were used as the negative control.
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Publication 2020

Most recents protocols related to «Butylene»

Example 7

Injection molded implants of succinic acid-1,4-butanediol-malic acid copolyester (Tepha lot 180333) with weight average molecular weight of 184 kDa, Tm=115° C., were prepared using an Arburg model 221 injection molder using the following conditions. The barrel temperature of the molder was increased from 70° C. at the feed zone to 170° C. at the end of the barrel. The mold temperature was maintained at 32° C. After molding, the implants were dried in a vacuum oven at room temperature for 48 hours, and tensile properties determined using an MTS test machine with a 2 inch/min cross head speed. Representative tensile properties of the implants were as follows: Young's Modulus 0.66 GPa (96,600 psi), Yield Strength 49.2 MPa (7,140 psi) and Break Stress of 71.7 MPa (10,400 psi).

Example 8

Interference screws with a diameter of 7 mm and length of 20 mm were injection molded from succinic acid-1,4-butanediol-malic acid copolyester (Tepha lot 180333), and from the same copolyester after blending with 50 wt. % beta-TCP (tri-calcium phosphate). The screws were formed using a similar procedure to that described in Example 7. After injection molding of the screws, the intrinsic viscosity of the compositions was essentially identical to that of the starting materials, indicating little loss of weight average molecular weight during injection molding occurred. The torsional strength of the screws was determined by embedding the tip of the molded screws in epoxy resin and measuring the maximum torque achieved by the screwdriver before failure of the screws. The average of three screws tested for the copolyester alone gave a value for torsional strength of 15.0 Ncm. The testing was repeated for the screws prepared from the blend, and the average value was 18.2 Ncm. For comparison, a commercial Arthrex Biointerference screw for implantation composed of PLLA (poly-L-lactic acid) was also tested. The Arthrex Biointerference screw has an average failure torque of 12.1 Ncm.

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Patent 2024

Example 1

Succinic acid-1,4-butanediol-malic acid copolyester (Tepha lot 180333) with weight average molecular weight of 184 kDa, Tm=115° C., (melt flow rate (MFR) at 190° C./2.16 kgf of 5 g/10 min) was dried under vacuum overnight to less than 0.01% (w/w) water. Dried pellets of the polymer were fed into an extruder barrel of an AJA (Alex James Associates, Greer, South Carolina) ¾ single screw extruder (24:1 L:D, 3:1 compression) equipped with a Zenith type metering pump (0.16 cc/rev) and a die with a single hole spinneret (0.026″, 2:1 L:D) under a blanket of nitrogen. The 4 heating zones of the extruder were set at 75° C., 165° C., 180° C. and 180° C. The extruder was fitted with a quench bath filled with water at 35° C. and set up with an air gap of 10 mm between the bottom of the spinneret and the surface of the water. Two 2-roll godets were positioned after the quench bath, followed by two sets of longitudinal hot convection chamber/2-roll godet combination. The temperatures of the hot convection chambers were set between 60° to 80° C., followed by 2-roll godets then a horizontal winder. Pellets of the copolyester were allowed to enter the heated extruder barrel, molten polymer passed through the barrel, entered a heated block followed by a metering pump then a single hole spinneret. The block, metering pump and the spinneret die were maintained at a constant temperature, preferably 180° C. Pump discharge pressure was kept below 1500 psi by controlling the temperatures and the speed of the metering pump. The resulting spun extrudate filament was free from all melt irregularities. The extrudate was quenched in a water bath, drawn through longitudinal ovens and wound on a horizontal tension controlled Sahm winder. The results of 3 trials with in-line orientation and shown in Table 1, together with the result of a fourth trial where the fiber was not oriented in-line, but rather off-line and 10 days after it had been extruded. From inspection of Table 1, it will be evident that the conditions used to prepare the monofilament fiber resulted in fiber with a tensile strength in the range of 434-518 MPa.

TABLE 1
Properties of monofilament fibers made from PBS copolymer
derived from 2-stage orientation in convention ovens
Trial#1#2#3#4
OrientationOnlineOnlineOnlineOffline
DelayNoneNoneNone10 days
Godet 1 (m/min)3.33.33.33.3
Hot Chamber 1 (° C.)62627070
Godet 2 (m/min)18.618.618.515
Hot Chamber 2 (° C.)75758080
Godet 3 (m/min)22212322.5
Orientation ratio (total)6.676.366.976.82
Fiber Diameter (mm)0.1780.1820.1830.172
Tensile Strength (MPa)452449434518
Break Elongation (%)46674124

Example 2

Succinic acid-1,4-butanediol-malic acid copolyester (Tepha lot 180333) with weight average molecular weight of 184 kDa, PD=2.83, Tm=115° C., (MFR 190° C., 2.16 kg, 5 g/10 min) was dried under vacuum overnight to less than 0.01% (w/w) water. Dried pellets of the polymer were fed under a blanket of nitrogen into the extruder barrel of a 2½″ American Kuhne single screw extruder (30:1 L:D, 3:1 compression) equipped with a Zenith type metering pump model HPB917, a die with 0.5 mm-8 hole spinneret and 8 heat zones. The 8 heating zones of the extruder were set between 40° C. and 200° C. The extruder was fitted with a quench bath filled with water at 35°-70° C. and set up with an air gap of 10 mm between the bottom of the spinneret and the surface of the water. Two 5-roll godets were positioned after the quench bath, followed by three sets of hot conduction chambers fed by godets in order to orient the fiber in multiple stages. The temperatures of the hot chambers were set up between 50° to 90° C. temperature. Another godet was positioned after the last chamber, and then a multi-position Sahm winder. The results from three trials are shown in Table 2. In comparison to the results shown in Table 1, the use of multi-stage incremental orientation of the fiber and conductive chambers instead of standard conventional non-liquid chambers resulted in monofilament fiber with substantially higher tensile strengths of 779-883 MPa.

TABLE 2
Properties of monofilament fibers made from PBS
copolymer derived from multi-stage orientation in
conductive liquid chambers
Trial#1#2#3
OrientationOnlineOnlineOnline
Godet 1&2 (m/min)3.63.61
Hot Chamber 1 (° C.)555560
Godet 3 (m/min)14143.7
Hot Chamber 2 (° C.)808065
Godet 4 (m/min)2828.37.7
Hot Chamber 3 (° C.)858565
Godet 5 (m/min)3029.78.22
Orientation Ratio8.38.258.2
Diameter (mm)0.1690.1660.167
Tensile Strength (MPa)779752883
Break Elongation (%)2423.723
Young's Modulus2.8n.d.n.d.
(GPa)

Example 3

Succinic acid-1,4-butanediol-malic acid copolyester (Tepha lot 180333) with weight average molecular weight of 184 kDa, PD=2.83, Tm=115° C., (melt flow rate (MFR) at 190° C./2.16 kgf of 5 g/10 min), was dried under vacuum overnight to less than 0.01% (w/w) water. Dried pellets of the polymer were fed into an extruder barrel of an AJA (Alex James Associates, Greer, South Carolina) ¾″ single screw extruder (24:1 L:D). The extrusion barrel contained 4 heating zones, a metering pump and a spin pack assembly. The pellets were gravity fed into a chilled feeder section and introduced into the extruder with temperature profile set as follows: Chimney 40° C.-100° C., Spinneret 170° C.±30° C., Pump 170° C.±30° C., Block 170° C.±30° C., Zone 4 160° C.±40° C., Zone 3 150° C.±40° C., Zone 2 120° C.±50° C., Zone 1 30° C.-40° C., Feed Zone: Ambient temperature. The heated and homogenized melted resin from the extruder was fed into a heated metering pump (melt pump), and from the melt pump the extruded resin was fed into the heated block and the spinneret assembly. The spinneret had 30 holes with a capillary diameter of 0.200 millimeters and a L/D ratio of 2:1. (The spinneret may also be configured in other alternative manners. For example, the spinneret can be configured with capillary diameters from 0.150 to 0.300 millimeters (6 mil to 12 mil) and 15, 120 and 240 holes, as well as higher and lower diameters and numbers of holes.) Processing temperature profile ranges from 35° C. to 250° C. were used with pressures ranging from 200 to 5,000 psi in the barrel and 200 to 5,000 psi in the spin pack. As the molten filaments exited the spin pack they passed through a heated chimney collar that was 6-12 inches long and ranged in temperature from 40° C. to 100° C., and then through an air quench box. The spin pack was suspended vertically above a yarn take-up roll at a distance sufficient to allow crystallization of the molten filaments and application of spin finish lubricant. A spin finish solution of 25% polyethylene 25 glycol 400 (PEG400) in water was used to hold the filaments together to form a yarn bundle. The speed of the yarn take-up rolls (typically 3-18 meters per minute) was set in proportion to the flow rate of the molten filament to control the denier of the as spun yarn bundle. The as spun yarn bundle was then conveyed to a Lessona winder for offline later orientation or conveyed to a take-up roll for inline orientation on a series of cold and heated godet pairs and separator rolls. The spin finish can be reactivated by rewetting the yarn bundle with pure water, and the yarn drawn at ratios from 5 to 14× and temperatures ranging from 50° C. to 90° C. The tenacity and denier of the multifilament yarn produced is shown in Table 3.

TABLE 3
Properties of Multifilament Fibers made from PBS Copolymer
Prepared by Melt Extrusion
Break
Number ofElongationTenacity
FilamentsDenierLoad (Kg)(%)(gpd)
15 60 ± 100.50 ± 0.0516%8.3
30 63 ± 100.79 ± 0.0420%12.5
30152 ± 101.55 ± 0.0721%10.2
60309 ± 102.80 ± 0.1024%9.1

Example 4

Oriented yarn produced according to Example 3 and with properties shown in Table 3 was braided using 8 and 16 carrier Steeger braiding equipment to form the braid constructions shown in Table 4. The mechanical properties of the high strength braided sutures, determined according to USP 24, are also shown in Table 4. The examples include a braid formed as a tape (shown as the last example in Table 4.

TABLE 4
Mechanical Properties of Braids and
Tapes Prepared from PBS Copolyester
Mechanical Properties
Braid ConstructionTensileBreak
LotCoreSheathPickDiameterstrength,elongation
Numberdenierdeniercount(mm)(Kg)(%)
TE18-0082 × 15216 × 152480.60826.539
TE18-0103 × 63 16 × 63 580.38014.231
TE18-0101 × 60 8 × 60490.2464.326
TE18-021170.5 × 3.0*6240
Tape13 × 6 × 126
Suturedenier
*Tape dimensions of 0.5 mm thickness and 3.0 mm width

Example 5

Monofilament fiber (USP suture size 5/0) prepared according to the method of Example 2 was processed into knitted mesh according to the following procedure. Monofilament fibers from 49 spools were mounted on a creel, aligned side by side and pulled under uniform tension to the upper surface of a “kiss” 10″ roller. The “kiss” roller was spun while semi-immersed in a bath filled with a 10% solution of TWEEN® 20 lubricant. The TWEEN® 20 lubricant was deposited on the surface of the sheet of monofilament fibers. Following the application of TWEEN® 20, the sheet of fiber was passed into a comb guide and then wound on a warp beam. A warp is a large wide cylinder onto which individual fibers are wound in parallel to provide a sheet of fibers. Next, warp beams were converted into a finished mesh fabric by means of interlocking knit loops. Eight warp beams were mounted in parallel onto tricot machine let-offs and fed into the knitting elements at a constant rate determined by the ‘runner length’. Each individual monofilament fiber from each beam was fed through a series of 20 dynamic tension elements down into the knitting ‘guides’. Each fiber was passed through a single guide, which was fixed to a guide bar. The guide bar directed the fibers around the needles forming the mesh fabric structure. The mesh fabric was then pulled off the needles by the take down rollers at a constant rate of speed determined by the fabric ‘quality’. The mesh fabric was then taken up and wound onto a roll and scored ultrasonically with water, heat set in hot water, and then washed with a 70% aqueous ethanol solution. The knitted mesh produced with monofilament fiber from Example 2 had the following properties (as shown in Table 11 at time 0): burst strength of 22.668 kgf, thickness of 0.683 mm, and Taber Stiffness of 0.116.

Example 6

Spools of multifilament fiber prepared according to the method of Example 3 were processed into knitted multifilament mesh using the method described in Example 5.

Example 12

The in vitro degradation rate of an implantable mesh prepared from oriented monofilament fibers of succinic acid-1,4-butanediol-malic acid copolyester (prepared as described in Example 5) was studied by incubation of the mesh in phosphate buffered saline. The buffer solution contained 137 mM NaCl, 2.7 mM KCl, 9.8 mM phosphate and 0.05 wt % sodium azide and had pH 7.4 at 25° C. The prepared buffer solution was filtered through a 0.45 um filter (VWR Product # 10040-470) prior to use. Mesh samples were sterilized by exposure to ethylene oxide gas. Samples (2×2 in.) were placed in sterile containers covered in buffer solution and incubated in a shaker incubator at 50 rpm and at a temperature of 37° C. Buffer media was monitored monthly and changed if the pH was outside of the targeted value 7.4±0.2. At prescribed time points, the samples were removed from the buffer and rinsed with deionized water to remove buffer salts. The samples were then tested for mechanical properties and weight average molecular weight retention of the polymer by gel permeation chromatography (as further described in Example 15). The in vitro degradation data is shown in Table 5.

TABLE 5
Mechanical and Mw data for PBS mesh samples made from oriented PBS
monofilament fiber after incubation in phosphate buffered saline (pH 7.4) at 37° C.
TimePeakStdStrengthMw
pointThickLoadDevRetentionMwStd DevPoly-Retention
(weeks)(mm)(kgf)(kgf)(%)(kDa)(Daltons)dispersity(%)
00.69621.7731.034100.01740.95.26100.0
20.68921.1171.56697.01660.25.0895.4
40.69619.9231.14191.51600.24.9492.1
80.69219.5371.13589.71470.74.5884.2
120.70918.6301.04485.61340.84.3377.2

Example 13

The degradation rate of an implantable suture prepared from oriented monofilament fibers of succinic acid-1,4-butanediol-malic acid copolyester in vitro was studied by incubation of the suture in phosphate buffered saline. The initial properties of the suture are shown in Table 6, line 1 (t=0). The buffer solution contained 137 mM NaCl, 2.7 mM KCl, 9.8 mM phosphate and 0.05 wt % sodium azide and had pH 7.4 at 25° C. The prepared buffer solution was filtered through a 0.45 um filter (VWR Product # 10040-470) prior to use. Suture samples were sterilized by exposure to ethylene oxide gas. Samples (12 in. length) were placed in sterile containers covered in buffer solution and incubated in a shaker incubator at 50 rpm and at a temperature of 37° C. Buffer media was monitored monthly and changed if the pH was outside of the targeted value 7.4±0.2. At prescribed time points, the samples were removed from the buffer and rinsed with deionized water to remove buffer salts. The samples were then tested for mechanical properties and weight average molecular weight (Mw) retention of the polymer by gel permeation chromatography (as further described in Example 15). The in vitro degradation data is shown in Table 6.

TABLE 6
Mechanical and Mw data for oriented PBS suture samples after incubation in
phosphate buffered saline (pH 7.4) at 37° C.
TimePeakStdBreakStrengthMw
pointLoadDevElongationRetentionMwStd DevPoly-Retention
(weeks)(kgf)(kgf)(%)(%)(kDa)(Daltons)dispersity(%)
01.7930.00725.133100.01740.24.86100.0
21.8010.00925.120100.41670.84.9396.2
41.8100.01025.364100.91630.54.8493.6
81.7720.02025.31198.81551.55.7889.4
121.7360.02124.86696.81460.64.8583.1

Example 15

The properties of a monofilament knitted mesh prepared from a copolymer of 1,4-butanediol and succinic acid units (the “PBS” mesh), as described in Example 5, were compared to a commercial mesh, the “GalaFLEX mesh (Galatea Surgical, Lexington, Massachussets)” prepared from knitting of poly-4-hydroxybutyrate monofilament in an in vivo implantation study in rabbits. The weight average molecular weight of the PBS mesh fibers prior to implantation was 173 kDa. The PBS and GalaFLEX meshes were implanted in the dorsal, subcutaneous tissue of New Zealand White rabbits to evaluate the local tissue reaction, the degree of tissue in-growth and the changes in mechanical properties of the meshes over time in vivo. Six (6) female New Zealand White (NZW) rabbits were implanted with 6 mechanical (4×4 cm), 1 histological (2×2 cm), and 1 scanning electron microscopy (SEM) (2×2 cm) test articles per animal.

Prior to implantation, the rabbits (weighing at least 3.5 kg at implantation) were anesthetized by an intramuscular injection, followed by maintenance under isoflurane. Following anesthesia, the animals were injected subcutaneously with an analgesic. The surgical sites were prepared for implantation. An incision was made through the skin and the skin was resected laterally by blunt dissection to create a pocket. Three individual mechanical samples (4×4 cm) and 1 histo/SEM sample (2×2 cm) were implanted on each side of each animal, for a total of 8 specimens per animal. The specimens were implanted by placing the mesh flat along the back of the animal without folding or rolling and fixated with a Prolene suture at each corner. The skin was closed and a bandage was applied. The animals were returned to their respective cages, monitored for recovery from the anesthetic, and then monitored daily for general health.

At 4 and 12 weeks, three rabbits were euthanized from each group. The skin was reflected, the subcutaneous tissues were examined and the area around each implant was dissected free. The implanted meshes were recovered by dissection from the surrounding tissue. The explants were processed for histological, biomechanical and polymer testing. At each time point, half of the 4×4 cm implanted meshes (n=9) were tested for mechanical properties including the in-grown tissue. The other samples (n=9), were designated for mesh-only analyses and were tested following collagenase digestion to remove ingrown tissue and evaluate the residual strength of the residual polymeric scaffold. In this way, the mechanical properties of the mesh alone could be measured and compared to that of the combination of mesh and tissue in the composite.

For the mesh-only samples, the in-grown tissue was removed from the explanted samples using enzymatic digestion with collagenase. Previous testing demonstrated no impact of the collagenase enzyme on the mesh mechanical properties or Mw properties. Individual explanted mesh specimens were placed in a 50 mL Falcon tube containing 25 mL collagenase (type I) solution (1.0 mg/mL) in TESCA buffer (50 mM TES, 2 mM calcium chloride, 10 mM NaN3, pH 7.4, sterile filtered). The tube was placed in a shaker (50 rpm) and incubated at 37° C. overnight (˜17 h) to digest and remove tissue attached to the mesh specimen. After the incubation was complete, the specimens were removed from the tubes, residual tissue was manually removed from the explant taking care not to damage the mesh, and the meshes were rinsed with distilled water followed by 70% ethanol. Mesh specimens were blotted dry using a lint-free wipe.

Samples were tested for dimensions, relative stiffness (Taber tester), burst strength and evaluated for surface morphology via SEM. Comparison was made to non-implanted (T0) articles (n=9/group). Polymer degradation was further evaluated by Gel Permeation Chromatography (GPC). The host tissue response and degree of tissue remodeling were evaluated histologically

Example 17

A mesh suture was prepared using triaxial braiding from high strength monofilament PBS fibers. Spooled monofilament fibers of succinic acid-1,4-butanediol-malic acid copolyester extruded and oriented as described in Example 2 were unspooled and wound on braider bobbins. The bobbins were then loaded onto Herzog 4, 8, 16 and 24 carrier braiders. Additional spooled monofilament fiber was used to provide axial fiber in the mesh suture. The monofilament fibers were unspooled and threaded through the hollow axles of the horn gears, and all bobbin and axial fiber ends were pulled through the braiding ring to form the fell point. The braiders' bobbins were allowed to move along the braiding track, and the braid helix angle was adjusted to 15 degrees at 1 to 2 Picks Per Inch (PPI). The constructions (number of carriers and axial fibers used to prepare the hollow braids) and properties of the triaxial braided mesh sutures prepared with 100 μm, 150 μm, and 200 μm P4HB monofilament fiber are shown in Tables 14, 15 and 16. The tables show the outside (OD) and inside (ID) diameters of the mesh suture hollow braids. The width and thickness of the hollow braided mesh sutures were measured after the hollow braids had been squashed flat.

TABLE 14
Properties of Triaxial Hollow Braids Prepared with 100 μm PBS
Monofilament Fibers
Hollow Triaxial Braid
BraiderCircularFlattenedTensile
## PillarODIDWidthThicknessStrength
CarriersFibers(mm)(mm)(mm)(mm)(N)
420.80.41.20.447
841.00.61.50.499
1261.30.92.00.4149
1681.71.22.60.4200
24122.82.23.40.4297

TABLE 15
Properties of Triaxial Hollow Braids Prepared with 169 μm PBS
Monofilament Fibers
Hollow Triaxial Braid
BraiderCircularFlattenedTensile
## PillarODIDWidthThicknessStrength
CarriersFibers(mm)(mm)(mm)(mm)(N)
421.00.41.50.697
841.50.92.30.6199
1262.51.93.90.6291
1683.02.44.70.6389
24124.03.46.20.6584

TABLE 16
Properties of Triaxial Hollow Braids Prepared with 200 μm PBS
Monofilament Fibers
Hollow Triaxial Braid
BraiderCircularFlattenedTensile
## PillarODIDWidthThicknessStrength
CarriersFibers(mm)(mm)(mm)(mm)(N)
421.10.31.70.8129
841.60.82.50.8259
1262.51.73.90.8389
1683.52.75.40.8518
24125.04.17.80.8778

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Patent 2024
Poly (butylene adipate-co-terephthalate) (PBAT, MFR 4–6 g/10 min at 190 °C) was purchased from Xinjiang Blue Ridge Tunhe Chemical Industry Co., Ltd., Changji, China. Native corn starch containing 73% amylopectin and 27% amylose (purity 99%) was provided by Binzhou Jinhui Corn Development Co., Ltd., Binzhou, China. Stearic acid was obtained from Oledchemicals Industry, Kuala Lumpur, Malaysia. Citric acid (purity 99.5%), glycerol (purity 99.5%), tributyl 2-acetylcitrate (ATBC, purity 97%), and all other chemicals were supplied by Macklin Chemical Co., Ltd., Shanghai, China.
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Publication 2024
Native corn starch Meritena® 100 was provided by Brenntag (Bratislava, Slovakia). Its water content was around 12 wt% as determined by drying in the oven at 100 °C for 5 h. Poly(butylene adipate–co–terephthalate) (PBAT), grade Ecoworld™ 003 with MFI < 5 (according to DIN ISO 1133 [38 ] at 190 °C and 2.16 kg), was supplied by Jinhui Zhaolong Co. (Shanxi Xiaoyi, China). Natrified montmorillonite (Cloisite® Na+) with a cationic exchange capacity range of 80–95 mequiv/100 g was purchased from Southern Clay Products (Gonzales, TX, USA). Glycerol was obtained from Centralchem, Ltd. (Bratislava, Slovakia). Double distilled water was used for the preparation of all solutions.
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Publication 2024

Example 14

The elemental composition of the Succinic acid-1,4-Butanediol-Malic acid copolyester was analyzed by Proton Induced X-ray Emission (PIXE) at Elemental Analysis Inc. This method provides quantitative elemental composition of a material for inorganic elements sodium through uranium on the periodic table. The elements found are shown in Table 7. The polymer did not contain detectable heavy metals such as Tin, which is sometimes used in the manufacture of resorbable polymers such as poly-glycolide, polylactide and poly-glycolide-co-lactide. The following trace elements were detected: silicon 18.98 ppm, titanium 14.77 ppm, and zinc 5.967 ppm.

TABLE 7
PIXE Analysis of a Poly(butylene succinate) Polymer
ElementEnergyDet. LimitConcentration
Name(keV)95% Conf.MassError
Silicon1.7408.964 ppm18.980 ppm5.056 ppm
Titanium4.5112.362 ppm14.770 ppm2.057 ppm
Zinc8.6390.457 ppm 5.967 ppm0.544 ppm

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Patent 2024
Butylene Glycols malic acid Metals, Heavy poly(butylene succinate) poly(lactide) Poly A Polymers PPM 18 Protons Roentgen Rays Silicon Sodium Succinic Acid Titanium Trace Elements Uranium Zinc

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