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Hydroxyethyl Starch 480/0.7 Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: Hydroxyethyl Starch 480/0.7 Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 226632
    Product Name Hydroxyethyl Starch 480/0.7 Pharma Grade API
    Synonyms HES 480/0.7; Hydroxyethyl starch 480/0.7; Hetastarch-like hydroxyethyl starch
    Cas Number 9005-27-0
    Molecular Formula (C6H10O5)n with hydroxyethyl substituents
    Average Molecular Weight 480,000 Da
    Molar Substitution 0.7
    Degree Of Substitution 0.7
    Appearance White to off-white, odorless, free-flowing powder
    Solubility Soluble in water; practically insoluble in ethanol, acetone, and other organic solvents
    Ph 5.0 to 7.5 (1% w/v aqueous solution)
    Grade Pharma Grade
    Purity ≥ 99.0%
    Loss On Drying ≤ 5.0%
    Residue On Ignition ≤ 0.5%
    Heavy Metals ≤ 10 ppm
    Dosage Forms Tablet, Capsule, Granule, Injection
    Routes Of Administration Oral, Injectable
    Storage Conditions Store in a cool, dry, well-ventilated place; protect from moisture and light
    Shelf Life 24 months from date of manufacture when stored properly
    Packaging 25 kg net fiber drum with double polyethylene liners

    As an accredited Hydroxyethyl Starch 480/0.7 Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

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    Application of Hydroxyethyl Starch 480/0.7 Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    In production-scale injectable formulation, hydroxyethyl starch 480/0.7 pharmaceutical-grade API is dissolved in water for injection with sodium chloride 0.9% w/v under a nitrogen overlay in a 316L stainless steel jacketed vessel fitted with a bottom-mounted magnetic agitator. The dissolution cycle is maintained at 20–30 °C for 60–90 min to avoid shear-induced chain scission; the target final concentration is 6% w/v. Before sterile filtration, the solution is passed through a 0.45 µm polyethersulfone prefilter and then a 0.22 µm polyethersulfone sterilizing-grade membrane in a single-use capsule assembly. Filter integrity is verified by diffusion/bubble point testing in accordance with the filter manufacturer’s protocol and ASTM F838-20 bacterial challenge data. The filtered solution is filled into USP Type II glass bottles with chlorobutyl rubber closures and autoclaved at 121 °C with a target F0 ≥ 15 min. Load thermometric mapping is required; cold spots located in the lower shelf corners have shown delayed attainment of 121 °C, requiring load-specific dwell corrections. In-process viscosity measured by Ph. Eur. 2.2.9 falls typically within 4–10 mPa·s at 25 °C, and colloid osmotic pressure measured with a membrane osmometer equipped with a 20 kDa cutoff membrane is maintained in the 30–40 mmHg range. The pH is adjusted to 4.5–6.5 before terminal sterilization; alkaline excursions above 6.5 accelerate hydrolytic cleavage of the hydroxyethyl substituent and shift the molecular weight distribution below specification. Bacterial endotoxin content is checked per Ph. Eur. 2.6.14 and must remain below 0.5 EU/mL; subvisible particulates are checked per Ph. Eur. 2.9.19 after final sterilization. This application is the most quality-critical downstream use because the API is present as a parenteral colloid oncotic agent, not merely as a processing excipient.
    Critical quality attributes for HES 480/0.7 injectable solution
    ParameterIn-process range or limitMethod / equipment
    Appearanceclear to slightly opalescent, colorless to pale yellowPh. Eur. 2.2.2
    pH4.5–6.5Ph. Eur. 2.2.3
    Viscosity at 25 °C4–10 mPa·sPh. Eur. 2.2.9
    Colloid osmotic pressure30–40 mmHgmembrane osmometer, 20 kDa cutoff
    Bacterial endotoxin< 0.5 EU/mLPh. Eur. 2.6.14
    Subvisible particlescompliesPh. Eur. 2.9.19

    Lyophilized Injectable Matrices Demand Annealing Control Above Tg'

    During cycle development for lyophilized vials containing HES 480/0.7 as a bulking matrix, the collapse temperature of the frozen plug is determined by modulated differential scanning calorimetry per ASTM E1356-08(2014), however published Tg' data for this specific molar substitution are sparse. The formulation is aseptically filled into 10 mL tubing glass vials and loaded onto a shelf freeze dryer with a condenser capacity ratio of at least 1.5 times the total sublimation load. Freezing is performed on shelves ramped from 5 °C to −45 °C at 0.5–1.0 °C/min; an annealing step at −15 °C for 2–4 h is introduced only when the formulation contains crystallizable co-excipients such as mannitol. Primary drying is conducted at a shelf temperature of −20 °C and chamber pressure of 150 µbar, with a total primary drying time of 40–60 h for a 50 mL fill volume. The amorphous HES phase does not crystallize during annealing, which avoids the phase separation seen with dextran-containing matrices. If sodium chloride is present above 0.9% w/v, the collapse temperature is depressed and the primary drying shelf temperature must be lowered below −25 °C, or product structural collapse appears as a wrinkled cake at the vial bottom. Published data for this specific configuration is limited; therefore thermocouple mappings and freeze-drying microscopy are used on every new formulation before full-scale lyophilization.

    When HES 480/0.7 Binds Water in Aqueous Granulation Before Fluid Bed Drying

    When HES 480/0.7 is dissolved in purified water to form a binder solution for tablet granulation, the hydration step in a jacketed stainless steel vessel is held below 40 °C to prevent rapid viscosity build-up that blocks transfer lines. The binder solution is added at 2–5% w/w of dry granule mass through a peristaltic pump into a high-shear granulator with an impeller tip speed of 5–10 m/s and a chopper speed of 1500–3000 rpm. The wet mass endpoint is controlled by power consumption torque rather than fixed time; the target loss on drying is 12–18% w/w. Granules are discharged through a 2 mm sieve and dried in a fluid bed dryer with inlet air at 60–75 °C and product temperature not exceeding 45 °C. The resulting granules are compressed on a rotary tablet press using 18 mm round flat-faced tooling; tablet breaking force is measured per USP 〈1217〉 and disintegration per USP 〈701〉. At binder concentrations above 5% w/w, tablet disintegration time increases beyond 30 min in purified water at 37 °C, which is unacceptable for immediate-release formulations. Published data for HES 480/0.7 as a tablet binder is limited; the viscosity and swelling behavior of this high-molar-mass grade require formulation screening with reduced binder levels compared to starch 1500.A different set of processing constraints appears in hard gelatin capsule filling, where HES 480/0.7 is milled to a particle size distribution with d90 ≤ 75 µm and blended with 0.5–1.0% w/w magnesium stearate. The powder is filled on a dosator-type encapsulator with a pin compression thickness set to 10–12 mm and a powder bed density of 0.50–0.65 g/mL; because the material exhibits hygroscopic uptake above 60% RH, the capsule filling suite is maintained at 25 °C and 35–45% RH. Moisture sorption analysis per Ph. Eur. 2.2.32 is used to confirm that equilibrium moisture content stays below 5% w/w; otherwise brittle capsule shells and delayed disintegration are observed. Final capsules are tested for content uniformity per USP 〈905〉 and dissolution per USP 〈711〉. Direct compression without granulation is not recommended for this grade because its high elastic recovery produces capping and weight variability on high-speed rotary presses. Published data for HES 480/0.7 in capsule formulations is limited, and pilot-scale trials must verify fill weight stability over extended run times.

    Oral Suspension Granule Hydration and Sedimentation Control

    For oral granule powders intended for reconstitution into suspension, HES 480/0.7 is dry-blended with sucrose, sodium citrate, and a preservative in a bin blender for 20–30 min at 12 rpm. The powder is granulated with purified water in a low-shear planetary mixer until the wet mass reaches a consistency suitable for extrusion through a 1 mm screen. The dried granules are filled into sachets; when reconstituted to 100 mL with potable water, the hydrated polymer develops an apparent viscosity of 50–200 mPa·s at 25 °C when measured with a Brookfield viscometer at 50 rpm. This viscosity retards sedimentation of the dispersed active pharmaceutical ingredient and provides a measurable pourability window of 10–15 s through a standard 10 mL oral dosing cup. The pH is buffered to 3.5–5.5 to avoid hydrolysis of the hydroxyethyl substituent under storage; real-time stability at 40 °C and 75% RH for 6 months is used to confirm that viscosity loss remains below 15% of initial. Published data for this specific HES grade in oral suspension granules is limited; the apparent viscosity range must be verified with each active pharmaceutical ingredient because ionizable actives can alter hydration kinetics.
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    Certification & Compliance
    More Introduction

    Hydroxyethyl Starch 480/0.7 Pharma Grade API is a hydroxyethylated amylopectin derivative obtained by controlled alkaline etherification of waxy maize or potato starch with ethylene oxide. The model identification encodes two critical structural specifications: a nominal weight-average molecular weight of 480,000 Da and a molar substitution of 0.7 hydroxyethyl groups per anhydroglucose unit. The substituted polymer is cold-water-soluble and does not form firm gels on cooling in neutral aqueous media, in contrast to unmodified amylose-containing starch. The API is supplied as a white to off-white, free-flowing powder and is used in oral solid dosage forms as a soluble binder, while in injectable preparations it functions as a colloid-active polymer after dissolution, depyrogenation, and terminal sterilization. Pharmacopoeial control includes loss on drying by Ph. Eur. 2.2.32, residue on ignition by Ph. Eur. 2.2.35, bacterial endotoxins by Ph. Eur. 2.6.14, and elemental impurities by USP 232/233 under ICH Q3D.

    Table 1: Typical specification targets for Hydroxyethyl Starch 480/0.7 Pharma Grade API.

    Nomenclature descriptorHES 480/0.7
    Weight-average molecular weight, Mwnominal 480,000 Da; common range 450,000–550,000 Da
    Molar substitution0.62–0.78
    Appearancewhite to off-white powder
    pH of 6% aqueous dispersion5.0–7.0
    Loss on drying5.0% w/w
    Residue on ignition2.0% w/w
    Particle size, D90150 µm for granulation-grade material
    Bacterial endotoxins, parenteral-grade lots0.25 EU/mg
    Test method referencesPh. Eur. 2.2.32, Ph. Eur. 2.2.35, Ph. Eur. 2.6.14, USP 232/233

    What Limits Direct Aqueous Granulation Performance at 480/0.7?

    In wet granulation, aqueous solutions of this grade develop higher extensional viscosity than povidone K30 or hydroxypropyl cellulose at equivalent solids. The molecular-weight fraction above 1,000,000 Da is primarily responsible for interparticulate bridge strength but also for delayed wetting of dry powders. Production-scale experience indicates that a binder solution of 3–8% w/w hydroxyethyl starch in purified water is generally suitable for lactose–microcrystalline cellulose blends, but the binder addition rate during high-shear granulation must be reduced as solution viscosity exceeds 150 mPa·s at 20 °C. A high-shear granulator operating at impeller tip speeds of 4–6 m/s and chopper speeds of 1,500–3,000 rpm can produce acceptable granule size distribution if the wet mass is not over-massed. Over-granulation produces dense, slow-disintegrating granules; disintegration time of the final tablet is evaluated according to Ph. Eur. 2.9.1 or USP 701. If final tablet hardness exceeds 80 N, the formulation may require a wicking disintegrant such as croscarmellose sodium at 2–5% w/w to maintain disintegration below 15 min.

    Encapsulation with the 480/0.7 grade as a binder in wet-massed or roller-compacted granules requires moisture content to be brought below 4% w/w before filling. Residual moisture above this threshold increases tackiness on dosator pins and tamping pins during automatic capsule filling, particularly on machines operating above 60,000 capsules/h. The API particle-size distribution should have a D90 below 100 µm for uniform die filling; larger particles segregate in the feed frame and contribute to weight variation beyond 2% RSD. When the grade is used as a dry binder for direct compression, its plastic deformation behavior is insufficient at pressures below 150 MPa; a co-processed excipient or a harder filler such as dibasic calcium phosphate anhydrous is normally required. Tablet tensile strength can be evaluated by the diametral compression method described in USP 1217 or Ph. Eur. 2.9.8.

    Injectable Formulation Constraints and Endotoxin Control

    Parenteral use of Hydroxyethyl Starch 480/0.7 requires depyrogenation and aseptic downstream handling. The API is not sterile at release; terminal sterilization of the finished solution is performed by steam sterilization at 121 °C for 15 min or by autoclaving cycles validated to a sterility assurance level of 10⁻⁶ according to Ph. Eur. 5.1.1 and ISO 14937. The pH of the formulation should be adjusted to 5.0–7.0 before terminal sterilization because acidic pH accelerates hydrolytic cleavage of the α-1,4-glycosidic backbone. Hydroxyethyl substitution on the C2 and C6 positions inhibits amylase degradation, but steam sterilization can reduce the weight-average molecular weight by up to 15–25%; the finished-product molecular weight distribution is therefore controlled by size-exclusion chromatography with multi-angle light scattering. Endotoxin control is exercised at the API level using the Limulus amebocyte lysate method of Ph. Eur. 2.6.14 or USP 85, with a commonly applied API acceptance criterion of ≤0.25 EU/mg for parenteral-grade material. The formulated isotonic solution is typically 6% w/v in 0.9% sodium chloride. Published data for this specific configuration is limited beyond the approved prescribing information for finished hetastarch products. This grade is not interchangeable with HES 130/0.4 in volume replacement because the higher molar substitution and molecular weight impart longer intravascular persistence and greater plasma volume expansion per gram, but also alter renal handling and coagulation parameters. Avoid combination with strongly acidic buffers and high-energy heat cycles; oxidative chain scission lowers molecular weight and raises reducing end groups.

    When Wet Granulation Is Replaced by Roller Compaction

    Roller compaction of HES 480/0.7-containing formulations shifts the critical process parameter from binder solution viscosity to ribbon solid fraction and post-compaction granule friability. The material is not sufficiently compressible to serve as the sole binder when roller compaction is operated below 0.65 solid fraction; ribbons with lower density crumble into fines and increase the fraction below 125 µm. A suitable formulation includes microcrystalline cellulose at 20–40% w/w and magnesium stearate at 0.5–1.0% w/w; the stearate should be added pre-blend only after the starch component has been deagglomerated. Published data for this specific configuration is limited, so ribbon density and granule particle-size distribution should be characterized using USP 429 and Ph. Eur. 2.9.31. The dissolution rate of HES 480/0.7 tablets can be determined using USP 711 apparatus 2 at 50 rpm and 37 °C; because the polymer is fully water-soluble, dissolution is typically matrix-controlled rather than diffusion-limited, and release follows near zero-order kinetics when tablet porosity is below 0.15.

    Comparative Differentiation against Lower-Molecular-Weight Hydroxyethyl Starches

    The 480/0.7 grade occupies a different formulation and clinical position than HES 130/0.4 or HES 200/0.5. The higher molar substitution of 0.7 restricts enzymatic hydrolysis by α-amylase, so intramolecular persistence is longer than for a 0.4-substituted polymer at equivalent molecular weight. In solid dosage forms, this means the 480/0.7 grade can form stronger interparticulate bridges at lower binder concentrations but also requires more water to reduce viscosity to pumpable levels. The colloid osmotic pressure of a 6% solution of 480/0.7 is higher than that of a 6% solution of 130/0.4; however, the corresponding increased oncotically active fraction means dose reductions are usually required for patients with impaired renal function. From a compendial perspective, the grade is not automatically interchangeable with HES 130/0.4 or HES 200/0.5 monographs; each grade must be tested against the applicable monograph for identity, substitution pattern, molecular weight distribution, and bacterial endotoxins.

    Table 2: Comparative profile of selected hydroxyethyl starch grades.

    PropertyHES 480/0.7HES 130/0.4HES 200/0.5
    Nominal weight-average molecular weight480,000 Da130,000 Da200,000 Da
    Molar substitution0.70.40.5
    Relative susceptibility to α-amylase hydrolysislowerhigherintermediate
    Typical formulation roleoral granule binder; high-colloid volume expander after processingparenteral volume expander with shorter persistenceparenteral volume expander with intermediate persistence
    Interchangeabilitynot interchangeable with lower-Mw gradesnot interchangeable with higher-Mw gradesnot interchangeable with higher-Mw grades
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