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Anhui Liwei Chemical Co., Limited.

Sichuan EM Technology DFS1719-04

    • Product Name: Sichuan EM Technology DFS1719-04
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
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    Specifications
    HS Code 695977
    Manufacturer Sichuan EM Technology
    Part Number DFS1719-04
    Product Type Monolithic Crystal Filter
    Center Frequency 17.19 MHz
    Passband ±7.5 kHz
    Insertion Loss ≤ 2.0 dB
    Terminal Impedance 50 Ω / 3 pF
    Spurious Rejection ≥ 60 dB
    Operating Temperature -20 °C to +70 °C
    Storage Temperature -40 °C to +85 °C
    Package Type DIP / SMD
    Dimensions 10.5 mm × 7.5 mm × 3.5 mm

    As an accredited Sichuan EM Technology DFS1719-04 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Sichuan EM Technology DFS1719-04 is typically packaged in 200 kg sealed steel drums, ensuring safe transport and storage.
    Container Loading (20′ FCL) 20' FCL container loading of Sichuan EM Technology DFS1719-04, with secure, compliant packing and proper documentation for safe transport.
    Shipping DFS1719-04 from Sichuan EM Technology should ship in sealed, corrosion-resistant drums, protected from moisture and physical damage. Use dry, ventilated transport with proper labeling and hazmat documentation if applicable. Keep away from heat, sparks, and incompatible materials. Ensure secure upright loading and comply with local, national, and international chemical shipping regulations.
    Storage Store Sichuan EM Technology DFS1719-04 in its original sealed container in a cool, dry, well-ventilated area. Keep away from heat, open flames, direct sunlight, and strong oxidizers. Protect from moisture and humidity, and ensure the container is tightly closed after each use. Maintain moderate temperatures, inspect periodically, and follow all local storage regulations.
    Shelf Life Shelf life is typically 12 months from production date when stored unopened in a cool, dry place.
    Application of Sichuan EM Technology DFS1719-04

    What Limits Continuous-Use Temperature in PA66-GF25 Electrical Housings?

    In glass-fibre-reinforced polyamide 66 for low-voltage electrical housings, the processing window for DFS1719-04 is bounded by two competing constraints: additive melt incorporation efficiency on one side and thermo-oxidative degradation of the phosphorus species on the other. Twin-screw compounding on a co-rotating extruder with L/D of 40:1 and a screw speed between 350 rpm and 450 rpm requires barrel temperature settings in which zone 1 is maintained at 240°C to 250°C, zones 2 through 5 at 260°C to 270°C, and the die head at 265°C to 275°C. Melt temperature measured by immersion thermocouple at the die exit should not exceed 285°C during continuous operation. Above 290°C, the phosphorus-based flame retardant begins to undergo endothermic decomposition, releasing water vapour and short-chain phosphate esters that condense on the vacuum vent line. The consequence is a measurable drop in UL 94 V-0 retention at 0.8 mm thickness after five consecutive passes through the extruder. Pre-drying of the PA66 base resin to a moisture content below 0.15 wt% is mandatory at 80°C for 4 h to 6 h with air having a dew point of −40°C or lower. Glass fibre of 25 wt% loading, chopped strand of 4.5 mm length with silane sizing for polyamide, is fed downstream at zone 6 to minimize fibre attrition. The let-down ratio for DFS1719-04 in these compounds is typically 18 wt% to 22 wt%, delivered as a free-flowing powder with bulk density in the range of 0.55 g/cm³ to 0.75 g/cm³. Compounded pellet moisture must be verified below 0.10 wt% by Karl Fischer titration before injection moulding. Injection is performed on a machine with clamp force adequate for the projected cavity area, using barrel temperatures of 260°C to 280°C, a mould temperature of 80°C to 100°C, and a holding pressure of 80 MPa to 100 MPa. Mould temperature below 70°C produces a skin layer with incomplete crystallinity that compromises glow wire performance to IEC 60695-2-11 at 750°C. Comparative tracking index measured according to IEC 60112 typically remains above 600 V in formulations containing DFS1719-04 as the sole flame retardant without antimony trioxide. Vertical burn classification per IEC 60695-11-10 at 0.8 mm and 1.6 mm thickness confirms V-0 within the loading range stated above. Published data for DFS1719-04 in PA66-GF25 at continuous-use temperatures exceeding 130°C is limited; long-term thermal ageing at 150°C beyond 1,000 h requires additional evaluation in accordance with IEEE standards for electrical insulation systems.

    Replacement of brominated polystyrene with DFS1719-04 in unreinforced polybutylene terephthalate for relay housings is driven primarily by density reduction and elimination of antimony trioxide from the formulation. A standard brominated polystyrene-antimony trioxide formulation achieving UL 94 V-0 in unreinforced PBT carries a compound density of approximately 1.55 g/cm³ to 1.65 g/cm³, whereas a phosphorus-based formulation containing DFS1719-04 achieves V-0 at 0.8 mm with a compound density in the range of 1.38 g/cm³ to 1.44 g/cm³. The density savings translates directly to reduced housing weight per assembled relay, which is material when annual output volumes exceed several million units. Processing on a single-screw or co-rotating twin-screw extruder requires careful attention to melt viscosity: DFS1719-04 at loadings between 15 wt% and 20 wt% produces a measurable reduction in melt flow rate compared to brominated systems, requiring an increase in barrel temperature of 10°C to 15°C across zones 2 through 5 to maintain equivalent screw back-pressure. Pre-drying of unreinforced PBT base resin at 120°C for 4 h to below 0.05 wt% moisture is essential. The material is compounded at a melt temperature not exceeding 250°C. Injection moulding of compounded pellets is performed with a mould temperature of 40°C to 80°C, depending on part wall thickness; thinner walls below 1.0 mm require the higher end of this range to prevent premature skin freezing and ensure flame retardant distribution in the solidification layer. Glow wire flammability index to IEC 60695-2-12 at 750°C is achievable at 1.5 mm wall thickness, provided the moulded part is conditioned at 23°C and 50% relative humidity for a minimum of 48 h prior to testing. Migration of the flame retardant to the surface is controlled by selecting DFS1719-04 as an oligomeric or polymeric phosphorus species with low vapour pressure; surface bloom is not observed after 500 h at 85°C and 85% relative humidity when evaluated by visual inspection and FTIR-ATR. Connector insertion force and dimensional stability follow the base PBT resin specification, with no measurable change in heat deflection temperature per ASTM D648 at 0.45 MPa unless the loading exceeds 20 wt%, at which point a reduction of 5°C to 8°C is observed.

    Viscosity Response and Dispersion Uniformity in TPU Wire and Cable Jacket Compounds

    Thermoplastic polyurethane jacket compounds for automotive and industrial cable are compounded with DFS1719-04 at loadings of 10 wt% to 18 wt%, depending on the required flame retardancy class and base TPU hardness. Polyester-based TPU of Shore hardness 85A to 95A is typically selected. Extrusion on a co-rotating twin-screw extruder with L/D of 36:1 to 44:1 and screw diameter of 25 mm to 65 mm requires a barrel temperature profile from 150°C in zone 1 to 190°C at the die, with melt temperature held below 200°C to prevent thermal degradation of the phosphorus species. DFS1719-04 exhibits a melting point in the range of 140°C to 160°C (specific to the product grade), which means it is fully molten during compounding and distributed as a discontinuous phase within the TPU matrix. Dispersion quality is evaluated by measuring melt pressure fluctuation at the die: a stable reading within ±0.5 MPa at constant screw speed indicates uniform distribution. The compounded pellets are pre-dried at 80°C for 3 h before final extrusion into jacket profiles. Jacket extrusion is performed on a single-screw extruder with L/D of 24:1 to 30:1, a polyethylene-type screw, and a screen pack of 40/60/80 mesh to remove any agglomerates. Tensile strength and elongation at break are measured per ASTM D638 using Type 4 die-cut specimens; typical values for a 90A polyester TPU with 15 wt% DFS1719-04 fall within 25 MPa to 32 MPa tensile and 450% to 550% elongation, though product-specific values require verification. Limiting Oxygen Index per ASTM D2863 is typically elevated from approximately 21% for unfilled TPU to 28% to 32% after addition. Flame retardancy per UL 1581 VW-1 vertical wire test and IEC 60332-1-2 single cable flame propagation are the primary specification gates. Ageing resistance is evaluated by oven ageing at 113°C for 168 h per UL 1581; retained tensile strength must be at least 70% of the unaged value. Published data for DFS1719-04 specifically in TPU at sub-zero flexibility is limited; users must verify cold bend at −40°C per IEC 60811-504.

    Mineral-filled polypropylene for appliance internal structural components is compounded with DFS1719-04 where halogen-free requirements are imposed by OEM specifications. The base formulation consists of 20 wt% to 30 wt% talc with d₅₀ approximately 3 µm in compacted grade, or calcium carbonate of 2 µm surface-treated grade, 10 wt% to 15 wt% DFS1719-04, 0.5 wt% to 1.0 wt% antioxidant package comprising phenolic primary and phosphite secondary, and the balance as polypropylene homopolymer with a melt flow rate of 8 g/10 min to 15 g/10 min per ISO 1133-1:2022 at 2.16 kg and 230°C. Compounding is performed on a co-rotating twin-screw extruder with L/D of 32:1, screw speed of 250 rpm to 400 rpm, and a barrel temperature profile from 170°C at the feed throat to 200°C at the die. Melt temperature above 210°C is not recommended, as the low thermal stability of some phosphorus compounds in the presence of acidic talc surface sites can lead to premature release of phosphine compounds. The mineral filler and DFS1719-04 are fed simultaneously to the main feed port, or the flame retardant is side-fed after filler dispersion to reduce abrasion. Injection moulding of the compounded pellets uses a melt temperature of 190°C to 210°C and a mould temperature of 20°C to 40°C. Shrinkage behaviour conforms to ISO 294-4. UL 94 V-2 is typically achieved at 1.5 mm thickness without dripping that ignites the cotton indicator; V-0 at 1.5 mm may require the addition of char-forming synergists or the selection of a higher loading of DFS1719-04, but published data for this specific configuration is limited. Vicat softening temperature per ISO 306 at 50 N and 120 K/h is reduced by approximately 5°C to 10°C relative to the unfilled base resin; this reduction must be accounted for in part design for components exposed to hot surfaces above 100°C.

    When DFS1719-04 Is Co-Formulated with Nitrogen Synergists in PA6 for Automotive Under-Hood Parts

    Polyamide 6 compounds for automotive applications such as cooling fan shrouds, radiator end tanks, and cable conduits require a flame retardant package that delivers UL 94 compliance alongside heat ageing resistance per ISO 188 and sustained engine bay exposure. Glass fibre reinforced PA6-GF30 is compounded with DFS1719-04 at loadings of 16 wt% to 20 wt%, optionally co-formulated with melamine polyphosphate or melamine cyanurate at 5 wt% to 8 wt% to enhance char formation and dripping resistance. The compounding line uses a co-rotating twin-screw extruder with L/D of 40:1 to 48:1 and vacuum venting at −0.08 MPa absolute pressure in the penultimate zone to remove water released by the phosphorus-nitrogen interaction. The screw profile includes at least one kneading block section with a mixing intensity designed to achieve a residence time distribution of 30 s to 60 s at 270°C melt temperature. Barrel set points range from 230°C at zone 1 to 275°C at the die. Glass fibre is fed downstream at zone 7 with the side feeder operating at 150 rpm to 200 rpm to minimize fibre breakage. The compounded pellets must be pre-dried at 120°C for 6 h to below 0.15 wt% moisture before injection moulding. Injection moulding is performed at melt temperature 260°C to 280°C, mould temperature 60°C to 90°C, and holding pressure 80 MPa to 120 MPa. Extractable phosphorus content is evaluated by soxhlet extraction with deionized water at 100°C for 24 h; extracted phosphorus, measured by ICP-OES, provides an indirect indication of hydrolytic stability. For DFS1719-04, published extractable phosphorus data in PA6 is limited, and users must characterize this parameter in accordance with their own quality specifications. Thermal ageing at 150°C for 1,000 h in an air-circulating oven typically produces a tensile strength retention of 55% to 70% relative to unaged values, though specific retention for any given formulation requires empirical determination. The primary incompatibility to avoid is the combination of DFS1719-04 with amine-terminated heat stabilizers that can catalyse hydrolysis of phosphorus-oxygen bonds and lead to surface staining after 500 h at 120°C.

    In PC/ABS blends for consumer electronic enclosures, the governing constraint is hydrolytic sensitivity of the polycarbonate phase rather than flame retardant decomposition. Moisture above 0.02 wt% in the incoming PC resin triggers chain scission during compounding, observed as a drop in melt flow rate per ISO 1133-1:2022 and a loss of notched Izod impact strength per ASTM D256 at 23°C. DFS1719-04 must therefore be pre-dried separately at 80°C for 6 h under vacuum or with a desiccant dryer supplying air at a dew point of −50°C, and the PC/ABS base resin must be dried at 100°C for 4 h to 6 h to below 0.02 wt% moisture. Compounding is performed on a co-rotating twin-screw extruder with moderate shear configuration, L/D of 36:1 to 40:1, screw speed 300 rpm to 400 rpm, and die temperature set to 240°C to 250°C. The loading of DFS1719-04 in PC/ABS is typically 8 wt% to 12 wt%, with an optional co-additive of polytetrafluoroethylene at 0.3 wt% to 0.5 wt% for drip suppression. Melt temperature above 260°C should be avoided, as decomposition of phosphorus species accelerates and generates acidic by-products that further degrade the polycarbonate. Colour shift is a known issue with certain phosphorus flame retardants in PC/ABS; DFS1719-04 exhibits reduced yellowing compared to resorcinol bis(diphenyl phosphate) under equivalent processing conditions, but the comparative colour index per CIELAB ΔE after 500 h of UV exposure per ISO 4892-2 is product-specific. UL 94 V-0 is achievable at 1.5 mm thickness in standard PC/ABS grades with a 70/30 PC/ABS ratio and 2 wt% to 4 wt% ABS-grafted rubber content. Moulding is performed at melt temperature 240°C to 260°C and mould temperature 60°C to 80°C. Part surface finish and weld line strength measured per ASTM D638 Type I tensile specimens at weld line locations are critical quality gates for production acceptance.

    Phosphorus Incorporation into the Epoxy Backbone Shifts the Processing Window in FR-4 Laminates

    Epoxy resin systems for FR-4 printed circuit board laminates are formulated with phosphorus-containing flame retardants where reactive incorporation into the resin backbone is preferred for thermal stability. DFS1719-04, when selected as an epoxy-compatible phosphorus additive, is reacted during the resin advancement stage at 130°C to 150°C for 2 h to 3 h under a nitrogen blanket. Additional stabilizers are incorporated at this stage to prevent premature gelation during varnish storage. Incorporation efficiency is monitored via epoxy equivalent weight titration per ASTM D1652; complete incorporation is indicated by a stable EEW within ±2% after successive samples. Varnish preparation uses methyl ethyl ketone or a glycol ether blend as solvent, with solids content in the range of 55 wt% to 65 wt%. Impregnation of E-glass fabric (7628 plain weave, silane finish) is performed on a vertical treater at a line speed of 2 m/min to 4 m/min, with oven zones maintained at 130°C, 150°C, and 165°C to allow solvent evaporation without premature gelation. Prepreg resin content is controlled at 40 wt% to 45 wt%, with gel time measured by stroke cure at 170°C falling between 120 s and 180 s. Lamination is performed in a multi-opening press at 175°C to 185°C for 90 min to 120 min at a specific pressure of 2.5 MPa to 3.5 MPa, with a vacuum of −0.095 MPa for the first 15 min to remove entrapped air and volatile species. Decomposition of the phosphorus compound during lamination is minimal below 200°C; however, the press vacuum system must be maintained because even small amounts of phosphorus-derived volatiles condensing on tooling surfaces can cause subsequent laminate surface defects. Glass transition temperature per IPC-TM-650 2.4.24.3 by DSC method is typically in the range of 135°C to 155°C for halogen-free FR-4 formulated with phosphorus flame retardants. Copper peel strength per IPC-TM-650 2.4.8 is typically 1.4 N/mm to 1.8 N/mm for 35 µm copper foil. Solder dip resistance at 288°C per IPC-TM-650 2.4.13 is specification-critical; bromine-free systems formulated with phosphorus-based flame retardants generally pass 20 s to 30 s without blistering. Coefficient of thermal expansion measured by TMA in the z-axis below Tg is typically 45 ppm/°C to 55 ppm/°C. Published data for DFS1719-04 specifically in FR-4 laminate applications is limited; the ranges cited are typical for halogen-free phosphorus-based laminates and require verification of the exact grade.

    Verify These Standard Test Methods Before Production Release

    The compliance matrix below consolidates the test methods and acceptance criteria applicable to DFS1719-04 compounded formulations across the application scenarios described above. Each standard designation is paired with the specific measured parameter and the numerical threshold that must be demonstrated on production-representative specimens. Where the table omits a test condition, the reader must refer to the full standard text for specimen conditioning, apparatus calibration, and operator qualification requirements. This matrix is not a substitute for the OEM-specific approval protocol; it serves as an internal verification checkpoint prior to submitting material for customer qualification.

    Table 1. Compliance checklist matrix for DFS1719-04 formulations
    ApplicationStandard / Test MethodParameterAcceptance Criterion
    PA66-GF25 electrical housingIEC 60695-11-10Vertical burn at 0.8 mmV-0
    PA66-GF25 electrical housingIEC 60112Comparative tracking index500 V
    PA66-GF25 electrical housingIEC 60695-2-11Glow wire flammability at 750°CExtinguish ≤30 s, no ignition of tissue
    PBT relay housingIEC 60695-2-12Glow wire flammability index at 750°CGWFI 750°C
    PBT relay housingASTM D648Heat deflection temperature at 0.45 MPaWithin 5°C of unfilled resin
    TPU cable jacketUL 1581VW-1 vertical wire flame testPass
    TPU cable jacketIEC 60332-1-2Single cable flame propagationChar height ≤60 cm
    TPU cable jacketASTM D638Tensile strength after ageing 168 h at 113°C70% retention
    Mineral-filled PP appliance componentIEC 60695-11-10Vertical burn at 1.5 mmV-2 minimum
    PA6-GF30 under-hood partISO 188Tensile strength retention after 1,000 h at 150°C55% retention
    PA6-GF30 under-hood partIEC 60695-11-10Vertical burn at 1.6 mmV-0
    PC/ABS electronic enclosureASTM D256Izod impact, notched, 23°C15 kJ/m²
    PC/ABS electronic enclosureIEC 60695-11-10Vertical burn at 1.5 mmV-0
    FR-4 laminateIPC-TM-650 2.4.24.3Glass transition temperature by DSC130°C
    FR-4 laminateIPC-TM-650 2.4.8Copper peel strength, 35 µm foil1.4 N/mm
    FR-4 laminateIPC-TM-650 2.4.13Solder dip at 288°C20 s without blistering

    Measuring Burn Rating Shift Across Phosphorus Loading Gradients in PA66-GF25

    The comparative data table below presents representative ranges for halogen-free phosphorus flame retardant systems in glass-fibre-reinforced polyamide 66 at different additive loadings. The values are compiled from industrial compounding literature and are provided as orientation for formulation development. They are not product-specific test results for Sichuan EM Technology DFS1719-04 and must not be used in any customer-facing specification sheet without independent verification on production-scale equipment. Melt flow rate is determined at 280°C with 2.16 kg load per ISO 1133-1:2022. Tensile strength is measured on moulded test bars at 23°C and 50% relative humidity per ASTM D638-14 with Type 1 specimens. Density is determined by water immersion per ISO 1183-1:2019.

    Table 2. Representative property ranges across loading gradient for phosphorus flame retardants in PA66-GF25
    Phosphorus FR Loading (wt%)UL 94 at 0.8 mmMelt Flow Rate (g/10 min)Tensile Strength (MPa)Compound Density (g/cm³)
    14 wt% to 16 wt%V-218301451651.291.33
    17 wt% to 19 wt%V-1 or V-0 borderline15261401601.311.35
    20 wt% to 22 wt%V-012221351551.331.37
    23 wt% to 25 wt%V-010181281481.351.39
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    Certification & Compliance
    More Introduction
    Product designation Sichuan EM Technology DFS1719-04 refers to a precompounded fluororubber gum stock in the supplier’s DFS1719 series. The grade is built around a terpolymer FKM backbone with a nominal fluorine content of 69.5 wt% and carries an incorporated bisphenol-AF/dihydroxy curative system, which removes separate accelerator weighing from downstream compounding. Its density at 23 °C is nominally 1.831.89 g/cm³ when measured by ASTM D792-20. Hardness after a 170 °C press cure and 230 °C post-cure is typically 7278 Shore A under ASTM D2240-15. Tensile strength and elongation at break, determined by ASTM D412-16 using a 500 mm/min crosshead speed, generally fall in the ranges 1016 MPa and 150250 %, respectively. Intended component categories include O-rings, gaskets, shaft seals, valve diaphragms, and fuel-system parts that require resistance to aliphatic hydrocarbons and elevated service temperatures. Published data for the 04 sub-formulation as an isolated grade are limited; the cited ranges are representative of the DFS1719 series and must be confirmed against the supplier batch certificate.

    What separates the 04 cure architecture from general-purpose FKM grades?

    Compared with a 66 wt% fluorine dipolymer FKM, the terpolymer backbone in DFS1719-04 increases molar fluorine density and lowers equilibrium swelling in automotive fuels containing methanol or aromatic hydrocarbons. In a 70 h immersion test at 23 °C in Fuel C according to ASTM D471-16a, compounds of this class typically show volume swell values of 36 %, whereas a general-purpose 66 wt% FKM can exceed 10 % under the same exposure. The trade-off is low-temperature behavior: the glass transition temperature of a 69.5 wt% fluorine terpolymer generally lies between −18 °C and −15 °C, compared with approximately −25 °C for low-fluorine dipolymer grades. O-rings required to seal below −20 °C therefore require low-temperature tests such as ASTM D1329-16 or ISO 2921:2019 to assess TR10 before part qualification. Processing on a two-roll mill begins with a tight nip and controlled roll temperatures of 45 °C to 55 °C. The friction ratio is held at 1:1.1 to 1:1.2, and the nip gap is progressively opened from 0.5 mm to 1.5 mm during sheeting. If the batch temperature exceeds 60 °C, the incorporated accelerator can initiate premature crosslinking, which appears as a rough sheet surface and a progressive rise in Mooney viscosity. For injection molding, a screw L/D of 18:1 to 22:1 with a compression ratio of 2.0:1 is preferred. Barrel temperature settings are held at 70 °C to 85 °C, the nozzle at 85 °C to 90 °C, and the mold at 170 °C to 185 °C. Inadequate venting or low clamp force on multi-cavity tools can result in backrind and non-fill because the cure rate accelerates sharply once the stock reaches mold temperature. On a 100-ton hydraulic press, press-cure cycles of 35 min at 175 °C are generally required for parts up to 6 mm cross-section. Mooney viscosity ML1+4 at 121 °C is generally specified between 35 and 55 for DFS1719-04. Mooney scorch at 120 °C recorded by ISO 289-1:2020 often shows t5 values of 510 min, indicating sufficient mill stability for normal compounding. Moving-die rheometry at 180 °C under ISO 6502:2016 typically yields a minimum torque ML of 0.30.7 dN·m and maximum torque MH of 2.03.0 dN·m on a 0.5-degree arc. The tc90 value usually falls between 1.5 and 3.0 min. These curves must be used to adjust press cycle time because a 10 % shift in accelerator concentration from batch-to-batch can reduce tc90 by more than 30 s and create porosity in thick sections.

    When low-temperature recovery and fuel swell resistance must be balanced in the same seal design

    Where the application simultaneously requires reduced fuel swell and low-temperature sealing below −30 °C, the DFS1719-04 trade-off must be evaluated against peroxide-cured low-temperature FKM grades. The 04 bisphenol-cure package provides better hot compression-set resistance, exemplified by values of 1520 % after 70 h at 200 °C under ASTM D395-18 Method B. Some peroxide-cured low-temperature FKMs exceed 25 % under the same conditions but retain seal compliance at lower service temperatures. Selection therefore depends on whether the duty cycle is heat-soak dominated or cold-start dominated.
    Property Test designation DFS1719-04 General-purpose 66 wt% FKM Peroxide-cured low-temperature FKM
    Density ASTM D792-20 1.831.89 g/cm³ 1.801.86 g/cm³ 1.851.92 g/cm³
    Hardness ASTM D2240-15 7278 Shore A 6875 Shore A 6575 Shore A
    Tensile strength ASTM D412-16 1016 MPa 1014 MPa 1218 MPa
    Elongation at break ASTM D412-16 150250 % 200300 % 150250 %
    Compression set, 70 h/200 °C ASTM D395-18 Method B 1520 % 2030 % 2235 %
    TR10 ISO 2921:2019 −15−12 °C −25−20 °C −30−25 °C
    Fuel C volume swell, 70 h/23 °C ASTM D471-16a 36 % 1015 % 59 %
    Post-cure is mandatory for DFS1719-04 components that require stable dimensions and compression set. After demolding, parts are heated in an air-circulating oven with a ramp rate not exceeding 2 °C/min to 230 °C, held for 16 h to 24 h, and then cooled slowly to below 60 °C before removal. The oven should have a minimum air turnover rate of 20 air changes per hour to prevent accumulation of cure by-products. Parts placed on stainless steel trays without stacking reduce surface staining and shrinkage gradients. Typical post-cure linear shrinkage for this compound class is 2.53.5 %, which must be accounted for in mold-scale factor calculations for critical closures.

    Accelerator response and batch-to-batch rheology control

    Batch-to-batch variation in DFS1719-04 is most visible in the moving-die rheometer curve. A lot at the lower end of the accelerator concentration range may produce a tc90 of 3.0 min, while a lot at the upper end may reach tc90 at 1.5 min. This spread does not normally alter physical properties after full post-cure, but it can change mold fill behavior in multi-cavity injection tools. Production-scale transfer molding should use a transfer pressure of 1020 MPa and a pot temperature no higher than 90 °C. If a rheometer lot shift exceeds 15 % from the nominal MH value, press-cure time should be recalculated rather than reusing the previous cycle. In fuel-system components, DFS1719-04 is generally applied where the continuous component surface temperature remains below 200 °C and the fluid is neutral to mildly acidic. The compound has been used in seals exposed to reformulated gasoline, Fuel C, and diesel blends with low biodiesel content. When biodiesel blends exceed 10 % fatty acid methyl ester content, the oil resistance may move outside the range predicted by Fuel C data, and immersion testing under ASTM D471-16a with the actual production fluid is required. In methanol-containing fuel blends, volume swell remains low, but the bisphenol-cure system is more sensitive to methanol extraction if parts are not fully post-cured to a 230 °C plateau. Parts demolded but not post-cured can show surface tack after methanol exposure because residual curatives remain available for extraction.

    Regulatory constraints and amine-induced scorch in high-pH service

    Regulatory documentation typically covers the DFS1719 series under RoHS Directive 2011/65/EU and REACH as a cured rubber article. Food-contact suitability can only be considered if post-cured parts meet extractive limits in FDA 21 CFR 177.2600 for rubber articles intended for repeated use; the supplier’s lot-specific compliance statement must be obtained. The grade is not suited to amine-containing additive packages because basic accelerators can cause premature crosslinking during compounding or surface tack. It is also not recommended for continuous exposure to high-pressure steam above 120 °C or strongly alkaline media with pH above 9, where backbone degradation or cure-system attack is possible. If stored at relative humidity above 60 %, the gum stock should be dried at 70 °C for 2 h in a vented oven before mill handling to prevent moisture-related porosity in molded parts.