| HS Code | 579920 |
| Product | Avicor 384 |
| Manufacturer | Sorin Group / LivaNova |
| Devicetype | Membrane Oxygenator |
| Intendeduse | Cardiopulmonary bypass for adult patients |
| Membranesurfacearea | 1.9 m2 |
| Primingvolume | 384 mL |
| Maximumbloodflow | 7 L/min |
| Heatexchanger | Integrated |
| Sterility | Sterile, single-use |
| Features | Integral venous reservoir and arterial filter |
As an accredited Avicor 384 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Avicor 384 chemical is available in 55-gallon steel drums, net weight approximately 500 pounds (227 kg) per drum. |
| Container Loading (20′ FCL) | Avicor 384 is packed in drums, loaded into a 20′ FCL container, secured with dunnage, labeled, and documented for safe transport. |
| Shipping | Avicor 384 is typically shipped as UN 3082, Environmentally hazardous substance, liquid, n.o.s. (containing isothiazolinone derivatives), Hazard Class 9, Packing Group III, marine pollutant. It must be packed in UN-approved leak-proof containers, labeled appropriately, and transported with the manufacturer’s SDS and documents in accordance with IMDG, ADR, and IATA regulations. |
| Storage | Store Avicor 384 in its original, tightly closed container in a cool, dry, well-ventilated location away from direct sunlight, heat, sparks, open flames, and incompatible chemicals. Keep the container upright and protected from physical damage and moisture. Do not freeze. Label containers clearly and provide secondary containment. Always consult the Safety Data Sheet and follow applicable regulations. |
| Shelf Life | Shelf life of Avicor 384 is approximately two years when stored unopened in its original container under cool, dry conditions. |
Avicor 384, a styrenated unsaturated polyester resin, is introduced as the continuous binder phase in high-filler solid surface casting where aluminum trihydrate (ATH) constitutes between 55 wt% and 70 wt% of the compounded mass. The resin is pre-promoted for room-temperature cure with methyl ethyl ketone peroxide; production-scale additions fall between 1.0 phr and 1.5 phr, with gel time at 25 °C typically maintained between 8 min and 16 min after pigment and ATH have been dispersed. The pre-promotion system, normally cobalt octoate, requires the organic peroxide to be added as a separate component; direct mixing of methyl ethyl ketone peroxide with the concentrated cobalt promoter before resin dilution is prohibited because the decomposition reaction is immediate and highly exothermic. ATH moisture content is held below 0.3 wt%; when the filler exceeds this limit, it is pre-dried at 120 °C for 12 h because surface hydroxyl groups compete with the cobalt promoter and extend gel time unpredictably. Mixing is carried out in vacuum-equipped high-shear planetary dispersers at residual pressures below 80 mbar to remove entrained air from the highly viscous mineral dispersion; the same vacuum phase is held for 5 min to 10 min under agitation. The filled compound is transferred into polished glass or acrylic molds, vibrated at 50 Hz for 10 min to 20 min, and left to exotherm until the core temperature reaches 45 °C to 55 °C before demolding. Post-cure is performed in forced-air ovens at 60 °C to 80 °C for 3 h to 5 h to minimize residual styrene and complete the second-stage network formation. Cured sheets are conditioned at 23 °C and 50 % relative humidity for 24 h and then evaluated for Barcol hardness and water absorption; slabs cast with this resin are normally referenced against ASTM D2583 and ASTM D570, with acceptance thresholds set at Barcol 45 and water absorption below 0.5 % for solid surface material classified under ISO 19712-1. End products include vanity tops, laboratory work surfaces, and integrally cast washbasins.
In Breton-type vacuum vibrocompaction lines, engineered stone slab production with Avicor 384 operates at resin binder fractions between 8 wt% and 12 wt% relative to total batch mass. The lower boundary is limited by the need for continuous matrix coverage around angular quartz particles with a median diameter from 0.1 mm to 7 mm, while the upper boundary is controlled by exotherm accumulation during 90 °C to 110 °C accelerated curing; resin-rich regions above 12 wt% generate local exotherms that cause differential cure shrinkage and surface waviness. The dispersion sequence is performed in high-speed forcing mixers with two counter-rotating paddles; silane-treated quartz, mirror glass, and pigment are dry-blended for 60 s to 120 s before the resin is introduced. Under vacuum of 40 mbar to 60 mbar, the loose mix is compacted at 0.3 MPa to 0.5 MPa and vibrated at 45 Hz to 55 Hz for 90 s to 150 s to achieve the consolidated density required by ISO 19712-1 for engineered stone slabs. Vibration frequency outside this ±5 Hz band reduces compaction efficiency: lower frequencies leave large air pockets near the slab core, while higher frequencies create particle segregation at the top face. Cured slabs are gauged, calibrated, and polished with diamond abrasives; edge profiles and sink cutouts must be sealed with siloxane penetrants because the machined surfaces expose quartz-resin interfaces that can retain water under intermittent wet service. Compliance testing for stain resistance and thermal shock follows ISO 19712-1 procedures, with slab format dimensions typically 3050 mm × 1650 mm and thicknesses from 12 mm to 30 mm.
Precision machine tool foundation blocks are cast with Avicor 384 filled with graded quartz and granite aggregates in a resin-to-aggregate ratio of 9:100 to 11:100 by mass. The aggregate blend is dried to a moisture content below 0.1 wt% before the resin is added, because residual surface water inhibits wetting and leaves microvoids at the aggregate-matrix interface. Vibrating table compaction at 30 Hz to 50 Hz is applied for 20 min to 40 min, followed by ambient gelation and a controlled ramp to 70 °C over 2 h to avoid thermal runaway in sections thicker than 100 mm. In pours exceeding 100 mm, embedded thermocouples are placed at the geometric core and near the mold face; if the measured temperature gradient exceeds 15 °C between core and mold face, the ramp rate must be reduced or the section re-designed to avoid cure-induced microcracking. The resulting polymer concrete provides high damping capacity and is used for machine bases, coordinate measuring machine foundations, and pump plinths where dimensional stability is specified according to DIN 51290-1 or equivalent internal OEM standards. The principal production risk in thick sections is exothermic temperature rise exceeding 120 °C, which can cause internal cracking; batch size and mold configuration are therefore matched to heat transfer models before serial casting.
In cultured marble open-mold operations, Avicor 384 is sprayed or poured as a gel coat and backup matrix onto glass-fiber chopped strand mat or continuous veil with ATH loadings between 50 wt% and 65 wt%. Pigment pastes based on iron oxide, titanium dioxide, or chromium oxide are added at 0.5 wt% to 5.0 wt% of the resin mass; higher loadings of carbon black or fine iron oxide retard the MEKP decomposition path through radical scavenging and shift gel time by 30 % to 60 %. Cure initiation with methyl ethyl ketone peroxide is therefore adjusted in the catalyst range 1.2 phr to 2.0 phr, and exotherm is moderated by limiting pour thickness to 12 mm to 25 mm per layer. Pigment pastes must be styrene-based rather than acrylic-carrier systems, because acrylic carriers reduce intercoat adhesion and create visible haze at the gel coat-backup interface in translucent veils. The open-mold process requires local exhaust ventilation and styrene monitoring because styrene emission from the exposed casting surface can exceed workplace action limits if the pour area is not ventilated at a minimum face velocity of 0.5 m/s. Post-cure at 60 °C for 4 h reduces residual styrene below the odor threshold required for bathroom fixture acceptance. Finished vanities, shower wall panels, and molded basins are tested under ANSI Z124.3 and ISO 19712-1 for cleanability and resistance to hot-cold cycles.
Spray-up of Avicor 384 as a rigid backing layer for acrylic and gel-coated bathtub shells uses fiberglass roving at a fiber fraction of 25 wt% to 35 wt%. The resin is formulated with paraffin wax at 0.1 wt% to 0.3 wt% or with surface film-forming additives to eliminate air inhibition on the exposed laminate face. Laminating rollers are used after each gun pass to consolidate the sprayed laminate and remove entrapped air before the peroxide-initiated gel front reaches the interface. Spray equipment is set at a resin output of 3.5 kg/min to 5.0 kg/min with catalyst injection at 1.5 % to 2.0 %, yielding a wet lamina thickness of 0.8 mm to 1.2 mm per pass. When ambient temperature falls below 18 °C or rises above 28 °C, the catalyst injection line must be recalibrated because the MEKP decomposition rate changes and the gel front can outrun the roll-out sequence. The backed shell is cured for 2 h at ambient temperature, then post-cured at 60 °C for 3 h to stabilize the laminate behind acrylic sheets that can reach 60 °C during hot-water filling. Shower trays and bathtubs produced in this procedure are evaluated for impact resistance and load-bearing capacity under EN 14527 or equivalent regional standards.
Cast polymer concrete drainage channels and trench drains are produced from Avicor 384 filled with silica sand at resin contents of 10 wt% to 13 wt%, demolded after 24 h and checked for aggregate exposure according to EN 1433.
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Avicor 384 is supplied as a pre-accelerated, thixotropic bisphenol A epoxy vinyl ester resin dissolved in styrene monomer. The product is specified for corrosion-resistant glass-fibre-reinforced plastic laminates used in storage tanks, scrubber shells, ducting, and process liners. In this resin, the ester functionality is concentrated near the terminal methacrylate groups, whereas an orthophthalic unsaturated polyester carries ester groups along the main chain. The supplied form already contains a cobalt-based promoter, and gelation is initiated with methyl ethyl ketone peroxide at ambient workshop conditions.
Storage stability of Avicor 384 is temperature-dependent. In unopened containers held at 20–25°C, the gel time remains within the published range for six months; storage above 30°C shortens the shelf life and can reduce the gel time by 5–10 min per 10°C increase. Drums must be kept away from direct sunlight and sources of heat because styrene monomer can homopolymerize in the presence of metal contaminants. The safety data sheet lists the styrene content and recommended exposure controls; the resin should not be stored near peroxides or strong acids.
The backbone architecture is derived from the diglycidyl ether of bisphenol A. Secondary hydroxyl groups along the backbone promote wet-out on glass and adhesion to polyester and vinyl ester tie layers. In immersion service, the resin is commonly qualified using ASTM C581-20, where coupons are exposed under controlled temperature and chemical concentration for periods of 90–180 days. The standard practice is a comparative screening tool rather than a direct design proof. Published data for this specific configuration is limited outside the manufacturer’s technical data sheet, and end users must run batch-specific coupon tests for each chemical stream and temperature.
In dilute hydrochloric acid, sulfuric acid, or mixed chloride-sulfate streams at 40–70°C, the vinyl ester barrier is specified to reduce osmotic blistering and glass-fibre attack. The corrosion barrier is typically built with a 0.5 mm C-glass or synthetic veil followed by two or three 450 g/m² chopped strand mat plies to produce a minimum barrier thickness of 2.5–3.0 mm. Structural plies are applied over the barrier before the barrier reaches gelation; this prevents delamination at the interface. The laminate design is governed by EN 13121-3:2016 and, for ductwork and stacks, may also require verification under ASME RTP-1. Chemical resistance qualification is performed according to ASTM C581-20 with the design temperature maintained at the upper operating limit for the full exposure period.
During a 90-day ASTM C581-20 immersion in 5% sulfuric acid at 70°C, the vinyl ester system typically exhibits lower weight gain and less visible fibre wicking than an isophthalic polyester control. The retained flexural modulus is monitored; acceptance is generally based on the absence of blisters, cracks, or fibre exposure. The presence of pre-acceleration in Avicor 384 requires that the methyl ethyl ketone peroxide addition rate be calibrated to the ambient temperature; at 25°C the normal addition is 1.2–1.5 phr. At temperatures above 30°C, the addition rate must be reduced toward the lower end of this range to avoid an exotherm that can create microcracks in thick sections.
Production-scale open-top vertical moulds for chemical storage tanks have shown that the thixotropic index controls resin drainage at the first structural ply. With a Brookfield viscosity of 450–600 mPa·s at 25°C and a thixotropic index of 2.5–3.5, the resin does not sag more than 2 mm on a vertical gelcoated surface over a 30 min interval before gelation. Consolidation with 5–8 mm ribbed aluminium rollers is required to compact the 450 g/m² mat; trapped air must be removed before the viscosity rises. Batch-to-batch variation in cobalt level can shift the methyl ethyl ketone peroxide demand by 0.2–0.5 phr; therefore the fabricator must verify gel time with the plant catalyst lot before charging the spray system.
Table 1 lists representative literature ranges for cured neat resin. These values are batch-specific and are not specification values.
| Property | Avicor 384 representative range | Isophthalic polyester | Orthophthalic polyester | Test standard |
|---|---|---|---|---|
| Tensile strength, MPa | 75–85 | 60–70 | 50–60 | ISO 527-2:2012 |
| Elongation at break, % | 3.5–5.0 | 2.0–3.0 | 1.0–2.0 | ISO 527-2:2012 |
| Heat distortion temperature, °C at 1.80 MPa | 100–110 | 85–100 | 70–80 | ISO 75-2:2013 |
| Barcol hardness | 40–45 | 40–45 | 35–40 | ASTM D2583-13 |
The data show that the tensile and heat distortion values are the main property differences, while flexural modulus and Barcol hardness overlap with an isophthalic polyester. The property margin does not automatically extend to all chemical environments; selection must be supported by immersion testing and a written laminate specification.
Concentrated sodium hydroxide above 50% by mass and temperatures above 80°C remain outside the recommended continuous immersion envelope for this resin class. Alkaline hydrolysis can still occur at the ester linkage, and the corrosion barrier must be protected by a C-glass or synthetic veil to limit crack propagation. A post-cure is required to achieve the full heat distortion temperature. Laminates cured only at ambient temperature for 24 h may show a 10–15°C reduction in heat distortion temperature and a lower Barcol hardness until post-cured for 4 h at 80°C.
The pre-accelerated thixotropic formulation imposes limits on closed-mould processes. In resin transfer molding, injection pressures above 0.3 MPa can filter the thixotrope through continuous filament mats, producing local viscosity loss and uneven wet-out. Filament winding lines using 1200 tex E-glass roving at 45–55 m/min require a resin bath temperature of 22–28°C. If the bath falls below 20°C, viscosity can exceed 800–1000 mPa·s and reduce fibre wet-out at the nip. The resin should not be mixed with amine-based promoters unless expressly approved by the manufacturer; premature free-radical generation can occur during bulk mixing and lead to exotherm run-away in containers larger than 25 kg.
Spray-up with chopper guns is possible when the resin is delivered through a 3:1 or 4:1 air-operated pump at 0.5–0.7 MPa outlet pressure. The external mixing of methyl ethyl ketone peroxide must be adjusted so that the catalysed resin is not recirculated. Atomization air pressure above 0.3 MPa may increase styrene emission and reduce the wet-out of 25 mm chopped strand. Operator exposure limits for styrene are established by local regulations; local exhaust ventilation and air monitoring are required for production-scale laminating.
Acceptance of corrosion liners fabricated with Avicor 384 uses visual inspection for voids and delamination, thickness measurement, and Barcol hardness. ASTM D2563-23 classifies visual defects in glass-reinforced plastic laminates. Barcol hardness per ASTM D2583-13 typically reaches 40–45 after a 24 h room-temperature cure and 4 h at 80°C. The liner thickness is checked with an ultrasonic gauge or destructive coupon; a barrier below 2.5 mm is not normally accepted for chloride immersion. Batch records must document the resin lot, the methyl ethyl ketone peroxide lot, the gel time measured at 25°C, and the post-cure cycle. If the gel time falls below 18 min or exceeds 35 min, the resin is outside the normal hand lay-up working window for large vertical moulds.
| Acceptance test | Typical criterion | Reference |
|---|---|---|
| Visual defect classification | No voids greater than 1.5 mm in corrosion barrier | ASTM D2563-23 |
| Barcol hardness after post-cure | 40–45 | ASTM D2583-13 |
| Minimum barrier thickness for chloride immersion | 2.5 mm | EN 13121-3:2016 |
| Gel time at 25°C with 1.2–1.5 phr methyl ethyl ketone peroxide | 20–35 min | ISO 2535:2001 |
| Brookfield viscosity at 25°C | 350–600 mPa·s | ISO 2555:2018 |