| HS Code | 750127 |
| Product Name | Hydroxyethyl starch 200/0.5 other active pharmaceutical ingredients Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Synonyms | HES 200/0.5; Pentastarch; Hydroxyethyl starch 200/0.5 |
| Chemical Name | Hydroxyethyl starch |
| Cas Number | 9005-27-0 |
| Molecular Formula | (C6H10O5)n with hydroxyethyl substituents |
| Molecular Weight | ~200,000 Da |
| Degree Of Substitution | 0.5 |
| Therapeutic Class | Plasma volume expander |
| Grade | Pharma Grade API |
| Appearance | White to off-white powder |
| Odor | Odorless |
| Solubility | Soluble in water; practically insoluble in ethanol and acetone |
| Ph | 5.0-7.5 (aqueous solution, typical) |
| Purity | ≥98.0% (typical) |
| Loss On Drying | ≤5.0% (typical) |
| Residue On Ignition | ≤0.5% (typical) |
| Heavy Metals | ≤10 ppm (typical) |
| Storage | Store in a cool, dry place, protected from light and moisture |
| Shelf Life | 24 months (typical) |
| Dosage Forms | Tablet, Capsule, Granule, Injection, Oral, Injectable |
| Route Of Administration | Intravenous; oral as listed in product description |
| Packaging | 25 kg fiber drum with inner polyethylene liner (typical) |
As an accredited Hydroxyethyl starch 200/0.5 other active pharmaceutical ingredients 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.
| Packing | Pharma-grade Hydroxyethyl starch 200/0.5 API supplied in 25 kg net double-lined polyethylene bags inside sealed fiber drums for oral/injectable use. |
| Container Loading (20′ FCL) | Secure 20′ FCL container loading: Pharma Grade Hydroxyethyl starch 200/0.5 API for tablets, capsules, granules, oral and injectable pharmaceutical applications. |
| Shipping | Hydroxyethyl starch 200/0.5 Pharma Grade API for tablet, capsule, granule, oral and injectable use is shipped in sealed, moisture-proof drums under clean, dry, controlled ambient conditions. Maintain cGMP/GDP compliance; avoid contamination, moisture, and temperature extremes. Label clearly and store away from oxidizers. Unless classified otherwise, transport as non-hazardous pharmaceutical cargo. |
| Storage | Store in tightly closed, original containers in a cool, dry, well-ventilated, secure area, protected from moisture, light, heat, and ignition sources. Maintain controlled room temperature (15–25°C) unless otherwise specified. Keep away from incompatible materials, contaminants, and food. Use appropriate PPE and maintain clean, labeled, segregated inventory with first-in, first-out stock rotation. For injectable-grade API, preserve container integrity and aseptic handling. |
| Shelf Life | Typically 24 months for Pharma Grade API when stored sealed, dry, protected from light, at controlled room temperature; confirm supplier stability data. |
In the intraoperative correction of acute hypovolemia where systolic pressure remains below 90 mmHg after a 20 mL/kg crystalloid challenge, a 6% w/v formulation of hydroxyethyl starch 200/0.5 in 0.9% sodium chloride is delivered through a 0.22 µm polyethersulfone filter into flexible, PVC-free polyolefin infusion bags. The release specification for the 6% w/v configuration requires 60 mg/mL hydroxyethyl starch 200/0.5, 9.0 mg/mL sodium chloride, a pH of 4.5–6.5, an osmolarity of 295–310 mOsmol/L, and a colloid osmotic pressure of 25–35 mmHg at 25 °C. Terminal product types are 250 mL and 500 mL ready-to-infuse bags. Release testing follows the current European Pharmacopoeia monograph for Hydroxyethyl Starch 200/0.5, Ph. Eur. 2.6.1 for sterility, Ph. Eur. 2.6.14 for bacterial endotoxins with a product-specific limit of ≤0.5 EU/mL, Ph. Eur. 2.9.19 for sub-visible particulates, and ICH Q3D for elemental impurities. Manufacturing is performed in a Grade D compounding area with transfer into a Grade A aseptic filling line under EU GMP Annex 1 (2022); the API is dissolved in Water for Injection at 18–25 °C using a low-shear overhead impeller at 35–50 rpm to avoid shear-induced molecular weight reduction, followed by pH adjustment with 0.1 M sodium hydroxide or hydrochloric acid and sterile filtration through two sequential 0.22 µm membrane filters before aseptic filling. The operational boundary excludes sepsis, creatinine clearance below 30 mL/min, severe coagulopathy, and pulmonary edema; the maximum daily dose is capped at 30 mL/kg in perioperative protocols, and the infusion line is not used simultaneously for citrated blood products without a saline flush to avoid calcium-chelate microaggregate risk in pumps with low flow velocity.
| Configuration | HES 200/0.5 addition ratio | Sodium chloride | pH range | Colloid osmotic pressure | Fill volume |
|---|---|---|---|---|---|
| 6% w/v isotonic infusion | 60 mg/mL | 9.0 mg/mL | 4.5–6.5 | 25–35 mmHg | 250 mL, 500 mL |
| 10% w/v hyperoncotic infusion | 100 mg/mL | 9.0 mg/mL | 4.5–6.5 | 60–80 mmHg | 250 mL, 500 mL |
Operationally, the adult circuit prime of 1500–1800 mL receives 300–500 mL of 6% w/v hydroxyethyl starch 200/0.5, equivalent to 17–33% of the total prime volume, with the remaining volume comprising isotonic crystalloid, 100 mL of 20% mannitol, and anticoagulant. The HES bag is a sterile 500 mL PVC-free polyolefin container with a Luer lock port; it is attached only after the crystalloid prime has wetted the hollow-fiber microporous polypropylene oxygenator and before sodium bicarbonate is fully mixed, because localized alkaline pockets can accelerate hydroxyethyl group hydrolysis. The primed circuit is recirculated at 2.0–3.0 L/min for 5–10 minutes through a 40 µm arterial line filter to remove microbubbles and particulate matter; the oxygenator is inspected for gas-phase separation under full pump flow before cannulation. Compliance sits with ISO 7199:2016 for the oxygenator and with the HES product release specifications under the European Pharmacopoeia. The process limitation is rheological, not osmotic: addition above 35% of pump prime volume delays fibrin polymerization in heparinized prime. Rotational thromboelastometry using ROTEM INTEM/HEPTEM assays shows reduced clot firmness at 10 minutes after protamine administration when the HES fraction exceeds 500 mL. Therefore the HES fraction is kept below 500 mL unless the perfusionist identifies hypoproteinemia with a plasma oncotic pressure below 20 mmHg. Terminal products are aseptic 500 mL pump prime bags ancillary to adult CPB circuits; neonatal circuits do not receive this addition ratio because the absolute HES dose per kilogram would exceed the institutional limit of 10 mL/kg.
Centrifugal granulocyte apheresis achieves red cell depletion by the introduction of 6% w/v hydroxyethyl starch 200/0.5 in 0.9% sodium chloride into the inlet line at a volumetric ratio of 1:6 to 1:10 with whole blood, with simultaneous trisodium citrate anticoagulant. The HES bag is attached through a sterile connection device to the apheresis kit inlet, and the peristaltic pump controls the HES-to-blood ratio; within the continuous-flow centrifugal chamber, erythrocyte rouleaux formation is accelerated, allowing the granulocyte-rich interface to migrate toward the collection port. Downstream production uses an optical interface detector to adjust plasma and red cell interface positioning at rotational speeds between 600 and 1200 rpm, depending on donor hematocrit and inlet flow rates of 30–70 mL/min. The terminal product is a 200–400 mL granulocyte concentrate intended for neutrophil transfusion under institutional protocols; the concentrate may carry residual HES and requires post-transfusion monitoring for volume overload. Compliance follows 21 CFR 606.40 for blood component collection establishments, 21 CFR 1271.10 for human cells, tissues, and cellular and tissue-based products, and AABB Standards for Blood Banks and Transfusion Services; the HES bag must remain part of a closed system during sterile docking to satisfy 21 CFR 606.65(a). This application is a process aid, not an approved HES drug indication in every territory, and the 10% w/v HES formulation is not used in apheresis because excessive rouleaux formation clogs the collection chamber and increases red cell carryover.
Whole blood withdrawal during acute normovolemic hemodilution is replaced at a 1:1 volume ratio with 6% w/v hydroxyethyl starch 200/0.5, typically 5–10 mL/kg removed into 250–450 mL CPDA-1 collection bags until the target hematocrit reaches 28–30%. The production sequence requires simultaneous infusion of HES 200/0.5 through an 18-gauge peripheral cannula while the autologous unit is drawn through a 16-gauge cannula; the CPDA-1 bag is placed on a calibrated shaker at 30–45 oscillations/min to prevent clot formation. Terminal products are labelled autologous whole blood units retained at ambient temperature for up to 6 hours in the operating theatre, with reinfusion initiated only after the surgical wound is closed or after a recorded loss threshold has been crossed. Regulatory control for this procedure includes 21 CFR 640.4 for whole blood collection containers, AABB Standards for Perioperative Autologous Blood Collection and Administration, and institutional blood conservation protocols aligned with ISO 9001:2015 process documentation. Operational boundaries include preoperative hemoglobin below 11 g/dL, severe coronary artery disease, active infection, and coagulation factor deficiency; the HES volume must not exceed 30 mL/kg, and the surgical team must be informed if the reinfusion sequence occurs more than 6 hours after collection because platelet function in the stored autologous unit declines.
Dimethyl sulfoxide toxicity in cell therapy freezing is reduced when 5% w/v hydroxyethyl starch 200/0.5 is combined with 5% v/v dimethyl sulfoxide and 10% v/v human serum albumin in the final cryoprotective cocktail. The HES 200/0.5 addition ratio is therefore 50 mg/mL in the cryoprotective medium, and the formulation is introduced at 4 °C to the washed hematopoietic progenitor cell pellet before controlled-rate freezing. Downstream production uses a controlled-rate freezer with an initial ramp of -1 °C/min to -40 °C, followed by transfer into vapour-phase liquid nitrogen at ≤-150 °C; the filled cryocyte bags are over-wrapped in an outer barrier film after sealing to prevent liquid nitrogen penetration. Terminal product types are cryopreserved hematopoietic progenitor cell units in 50–250 mL fluorinated ethylene propylene bags labelled according to ISBT 128; thaw is performed at the bedside in a 37 °C water bath with rapid dilution to remove DMSO. Compliance falls under 21 CFR 1271.10, 21 CFR 1271.11, and EU Directive 2004/23/EC, with batch release testing for sterility according to Ph. Eur. 2.6.1 and mycoplasma according to Ph. Eur. 2.6.7 before infusion. The operational boundary excludes patients with documented hydroxyethyl starch hypersensitivity; the program must reconcile cumulative HES dose with the patient’s renal function when multiple bags are thawed, because repeated colloid exposure in the cell therapy setting can produce cumulative volume and coagulopathy effects.
| Downstream application | Standard or code | Control parameter |
|---|---|---|
| Injectable volume replacement | Ph. Eur. 2.6.1, Ph. Eur. 2.6.14, Ph. Eur. 2.9.19, ICH Q3D | Endotoxin ≤0.5 EU/mL; sub-visible particles per monograph |
| Cardiopulmonary bypass prime | ISO 7199:2016 | 40 µm arterial line filter; ROTEM INTEM/HEPTEM |
| Granulocyte apheresis | 21 CFR 606.40, 21 CFR 1271.10, 21 CFR 606.65(a) | Closed sterile docking; HES-to-blood ratio 1:6–1:10 |
| Acute normovolemic hemodilution | 21 CFR 640.4, AABB Standards | Ambient storage ≤6 h; target hematocrit 28–30% |
| Hematopoietic progenitor cell cryopreservation | 21 CFR 1271.10, EU 2004/23/EC, ISBT 128 | Controlled-rate freezing -1 °C/min to -40 °C |
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Hydroxyethyl starch 200/0.5 is supplied as a pharmaceutical-grade semisynthetic amylopectin derivative in which the hydroxyl groups at the C2 and C6 positions of anhydroglucose units are partially substituted with hydroxyethyl groups. The model designation HES 200/0.5 encodes a nominal weight-average molecular weight of 200,000 Da and a molar substitution of 0.5. The product line includes HES 200/0.5 and co-supplied active pharmaceutical ingredients released for tablet, capsule, granule, injection, oral, and injectable dosage forms. Hydroxyethylation alters enzymatic recognition by α-amylase; the resulting polymer is not a simple native starch, and its colloid osmotic activity in solution is governed by molecular weight distribution, molar substitution, and the C2/C6 substitution ratio. Manufacturing documentation follows ICH Q7 for active pharmaceutical ingredients; injectable lots require endotoxin, bioburden, residual solvent, and molecular weight distribution data before release.
The pharma-grade designation means that each batch is released against a certificate of analysis containing chemical, physical, microbiological, and residue test results. The packaging configuration is selected according to route: injectable-grade material is supplied in double polyethylene bags inside sealed fibre drums; solid oral material may be supplied in LDPE-lined drums. Cross-contamination control follows 21 CFR 211 for finished pharmaceuticals and ICH Q7 for APIs.
The polymer is produced from waxy maize starch by controlled acid hydrolysis, followed by hydroxyethylation with ethylene oxide under alkaline conditions. The hydrolysis step sets the molecular weight target, while the hydroxyethylation step introduces short hydroxyethyl chains at the reactive hydroxyl positions. Residual ethylene oxide and ethylene chlorohydrin are controlled as process residues. The crude product is purified by precipitation or diafiltration and dried to a loss-on-drying specification of ≤5.0%. The resulting powder is white to off-white and freely soluble in water; solubility and clarity are monitored in release testing because incomplete purification can leave insoluble amylopectin aggregates that increase subvisible particulate counts in injectable formulations.
Molecular weight and molar substitution are not independent variables: a higher molar substitution at a given molecular weight will reduce the rate of α-amylase hydrolysis. For this reason, the 0.5 molar substitution represents a deliberate balance between intravascular persistence and tissue clearance. In solid dosage forms, the same balance affects dissolution and tablet disintegration because water penetration is faster through unsubstituted starch regions.
Release testing for injectable HES 200/0.5 starts with molecular weight distribution by size-exclusion chromatography coupled to multi-angle laser light scattering, using Ph. Eur. 2.2.30 as the system suitability reference. The nominal 200,000 Da weight-average molecular weight is not a single-chain mass but a distribution; control of the Mw/Mn ratio is necessary because high-molecular-weight fractions above 220,000 Da can increase solution viscosity and prolong renal retention. Molar substitution is determined after acid hydrolysis by gas chromatography, with an acceptance window of 0.45–0.55. The C2/C6 substitution ratio is measured by GC or NMR; published data for this specific configuration is limited, but a higher C2 substitution is understood to confer greater α-amylase resistance than C6 substitution. Residual ethylene oxide is controlled under Ph. Eur. 2.4.25 and ICH Q3C; bacterial endotoxin is measured by Ph. Eur. 2.6.14 with a typical parenteral limit of ≤0.5 EU/mg. Elemental impurities are controlled by ICH Q3D using ICP-MS.
| Parameter | Acceptance criterion | Test method/system |
|---|---|---|
| Appearance | white to off-white powder or granules | visual inspection |
| Molar substitution | 0.45–0.55 | GC after acid hydrolysis |
| Weight-average molecular weight | 180,000–220,000 Da | SEC-MALLS; Ph. Eur. 2.2.30 |
| Bacterial endotoxin (injectable) | ≤0.5 EU/mg | Ph. Eur. 2.6.14 |
| Loss on drying | ≤5.0% | Ph. Eur. 2.2.32 |
| Residual ethylene oxide | ≤1 ppm | Ph. Eur. 2.4.25 |
| Elemental impurities | ICH Q3D threshold limits | ICP-MS |
Water content is critical because HES 200/0.5 is amorphous and hygroscopic. Loss on drying above 5.0% may not indicate degradation, but it alters powder flow and can increase the risk of sticking to tooling. Moisture-corrected assay is performed by deducting loss on drying from the active assay result to prevent overestimation of potency.
In high-shear wet granulation, HES 200/0.5 is introduced as an aqueous binder solution at 5–10% w/w. The solution is sprayed onto a lactose-monohydrate and microcrystalline cellulose blend in a high-shear mixer with impeller tip speed between 4 and 8 m/s; granulation end point is controlled by torque rise rather than fixed time. Over-wetting produces agglomerates above 2 mm and increases fluid-bed drying at 60 °C beyond 40 min, which can lower tablet hardness through case hardening. Dried granules are milled through a 0.8 mm screen and blended with 0.5% w/w magnesium stearate; tablet hardness is maintained between 60 and 100 N for 10 mm round tooling. Capsule filling requires loss on drying below 5.0% because the amorphous starch derivative is hygroscopic and will plasticise gelatin or HPMC shells at RH > 60%. Injectable manufacturing dissolves HES 200/0.5 in water for injection and terminally steam-sterilises at 121 °C for 15 min; the cycle must be re-validated by SEC because autoclaving can shift the molecular weight distribution. Co-supplied APIs in the same pharma-grade line are released separately under ICH Q7 and cannot be treated as interchangeable without route-specific specifications.
Oral solid dosage forms use HES 200/0.5 in wet granulation at 2–5% w/w of the dry formulation as a binder. For extended-release matrices, higher levels up to 10% w/w are used with hypromellose or ethylcellulose to modify drug release. In capsule filling, granules are milled and filled by tamping or dosator systems; fill weight is adjusted to control weight variation under USP <905>, and moisture is kept below 5.0% to avoid shell deformation. For oral granules, the material is dry-mixed or wet-granulated and then passed through a 0.5–1.0 mm sieve; final blend uniformity is verified by pharmacopoeial sampling. Binding performance is not determined solely by molecular weight. The 0.5 molar substitution leaves sufficient unsubstituted regions for water uptake and film formation, while substituted regions suppress rapid enzymatic breakdown. In tablet formulations containing hygroscopic drugs, the binder solution is prepared at 25 °C and used within 8 h to avoid microbial proliferation. If the granulation is stored before compression, it should be held in sealed containers at RH < 40% to prevent moisture migration and the resulting loss of tablet hardness.
The use of HES 200/0.5 as a granulation binder does not automatically confer extended-release behaviour; drug release rate is governed by matrix polymer ratio, drug solubility, and compression force. A formulation with 10% w/w binder and a freely soluble drug may still release more than 80% of drug in 30 min under USP dissolution; therefore, dissolution testing should be used to confirm the desired profile.
The same HES 200/0.5 grade can be referenced for tablet and injection manufacturing, but the control envelopes differ by route. Solid oral use permits a wider bioburden envelope but requires powder flow and particle-size control to meet USP <905> uniformity of dosage units; injectable use demands bacterial endotoxin control, terminal sterilisation compatibility, and subvisible particulate limits under Ph. Eur. 2.9.19 or USP <788>. A lot released for oral granulation is not automatically suitable for parenteral compounding unless the batch meets the parenteral specification for endotoxin, bioburden, and residual solvent. For injectable filling, the solution is processed in an ISO 7 cleanroom with ISO 5 laminar airflow at the point of fill; terminal sterilisation by moist heat is validated according to Ph. Eur. 5.1.1. The presence of other active pharmaceutical ingredients in the product line does not imply pre-mixed formulation; each API is supplied with its own certificate of analysis and route-specific documentation.
The substitution pattern changes binder performance. Pregelatinised starch hydrates rapidly without cooking but is more sensitive to α-amylase and can swell unevenly when the granulation fluid is added too quickly. HES 200/0.5 in aqueous solution gives a more shear-thinning binder; its 0.5 molar substitution reduces the thickness of the hydrated layer compared with HES 200/0.62 and permits easier spray application. However, the same shear-thinning behaviour means nozzle clogging can occur if the solution is allowed to cool and viscosity rises; jacketed spray lines at 25–30 °C are recommended. Batch-to-batch variation in molecular weight distribution changes solution viscosity more than granule particle size; therefore, binder solution viscosity should be checked by Ph. Eur. 2.2.10 before spraying, and the addition rate adjusted to avoid a wet mass that forms ropes or sticks to the bowl wall.
Dry HES 200/0.5 is sensitive to moisture. Storage in sealed polyethylene-lined fibre drums below 25 °C and RH < 60% is specified; opened containers should be re-sealed immediately. At RH > 60%, moisture uptake plasticises the amorphous starch matrix and can increase particle adhesion during tableting. The product is incompatible with strong oxidising agents; compatibility with cationic APIs should be confirmed on a case-by-case basis because residual anionic groups can cause complex formation in solution. For injectable admixtures, electrolytes such as calcium chloride or high-phosphate buffers may alter the zeta potential and should be tested for precipitation before batch manufacture.
Injectable solutions of HES 200/0.5 generate colloid osmotic pressure because the high-molecular-weight fraction is retained within the vascular compartment. A 6% w/v solution generates a colloid osmotic pressure determined by the concentration and the molecular weight distribution; routine release data include SEC traces to confirm that the high-molecular-weight fraction is present. α-Amylase degradation assays are used to compare relative degradation rates: HES 200/0.5 degrades more slowly than HES 130/0.4 and more quickly than HES 200/0.62 under the same enzyme activities. The degradation products are cleared by renal and hepatic routes; this is why renal function monitoring is required. Regional regulatory restrictions apply to hydroxyethyl starch solutions; manufacturers must verify current label indications before formulation.
For injectable products, HES 200/0.5 is commonly formulated at 6% w/v in 0.9% w/v sodium chloride. The solution is filtered through 0.2 µm sterilising-grade filters before terminal sterilisation. Autoclaving at 121 °C for 15 min can decrease the weight-average molecular weight; therefore, SEC is repeated post-sterilisation to confirm that the molecular weight distribution remains within specification. Subvisible particulate testing according to USP <788> or Ph. Eur. 2.9.19 is required for injectable formulations; the acceptance criterion for particles ≥ 10 µm and ≥ 25 µm follows compendial limits. The product must not be combined with amine-containing APIs that can react with residual reducing end groups; such combinations require forced degradation studies to confirm absence of Maillard-type adducts.
Compared with HES 130/0.4, HES 200/0.5 exhibits a higher weight-average molecular weight and a higher molar substitution, which jointly reduce enzymatic hydrolysis and prolong intravascular retention. Compared with HES 200/0.62, the 0.5 molar substitution leaves fewer hydroxyethyl blocking groups, allowing faster α-amylase degradation and lower tissue accumulation. Compared with HES 450/0.7, HES 200/0.5 has a shorter circulating persistence and a lower tissue storage risk; however, all hydroxyethyl starch products require dose limitation and renal function monitoring in clinical use. In solid oral formulations, native starch, pregelatinised starch, and sodium starch glycolate are not interchangeable with HES 200/0.5: native starch has limited cold-water solubility, pregelatinised starch swells but lacks the same substituted amylase resistance, and sodium starch glycolate functions as a disintegrant rather than a binder or colloid. HES 200/0.5 is therefore selected when water-soluble binding, matrix formation, or colloid osmotic activity is required.
| Grade | Weight-average molecular weight (Da) | Molar substitution | Relative α-amylase degradation |
|---|---|---|---|
| HES 130/0.4 | 130,000 | 0.4 | Faster hydrolysis; lower tissue retention |
| HES 200/0.5 | 200,000 | 0.5 | Intermediate hydrolysis |
| HES 200/0.62 | 200,000 | 0.62 | Slower hydrolysis |
| HES 450/0.7 | 450,000 | 0.7 | Slowest hydrolysis; highest tissue persistence |
From a release perspective, oral and injectable versions are differentiated by the route-specific acceptance values for endotoxin, bioburden, and particulates, not by the HES grade name alone. A tablet binder lot may meet chemical identity and molar substitution but still fail injectable endotoxin testing; therefore, the intended manufacturing route must be fixed before lot selection.