Product Overview

The report provides detailed analysis essential for establishing a polidocanol production plant. It encompasses all critical aspects necessary for polidocanol production, including the cost of polidocanol production, polidocanol plant cost, polidocanol production costs, and the overall polidocanol production plant cost. Additionally, the study covers specific expenditures associated with setting up and operating a polidocanol production plant. These encompass production processes, raw material requirements, utility requirements, infrastructure needs, machinery and technology requirements, manpower requirements, packaging requirements, transportation requirements, and more.

Polidocanol Market Analysis: Demand and Supply Analysis, and Sourcing

Polidocanol is a nonionic surfactant that later became a medicine. It was first developed for use in industrial detergents and later became a widely used treatment for varicose and spider veins. Chemische Fabrik Kreussler has sold it under the brand name Aethoxysklerol since 1971, giving it a long history of use. Dermatologists, vein specialists, vascular surgeons, proctologists, and gastroenterologists all use polidocanol. Few medicines are used across so many medical specialties. Despite its simple chemical structure, it is used to treat varicose veins, spider veins, hemorrhoids, esophageal varices, and itching.

Polidocanol supply comes from a small pharmaceutical market and a much larger surfactant industry. Kreussler makes the reference product for Europe in Wiesbaden, Merz sells the American product under the brand name Asclera, and Boston Scientific sells the foam version as Varithena. The active ingredient market is small, with Agno Pharma, Maiva Pharma, Hänseler & Caesar, and Loretz involved in the supply chain. A polidocanol demand and supply analysis needs to consider the prevalence of venous diseases, the number of treatment procedures, the use of foam or liquid sclerotherapy, compliance with pharmacopoeial standards, and the quality difference between pharmaceutical-grade polidocanol and ordinary ethoxylates.

Polidocanol demand depends on the number of treatment procedures rather than prescriptions. A spider vein treatment uses up to 10 mL of dilute solution, while a foam treatment is limited to 15 mL, so the amount used per patient is small. Total demand depends on the number of sessions, with repeat liquid treatments usually scheduled one to two weeks apart and foam treatments at least five days apart. Clinic schedules, patient tolerance, the number of affected veins, and follow-up plans determine how often patients return. Demand for cosmetic treatments depends on disposable income, while treatment of larger veins depends on reimbursement policies. Buyers check assay, dioxane content, residual ethylene oxide, endotoxin, particles, and regulatory documents. Supplier approval takes time, so buyers rarely change suppliers. Each order also includes details about ampoule strength, pack size, shelf life, and required documents.

Summary of the Product, Grades, and Uses

Polidocanol does not have a single molecular formula because it contains a mixture of related compounds called homologs. Its general structure is C12H25(OCH2CH2)nOH, consisting of a lauryl alcohol chain attached to a polyethylene glycol chain, with an average polymerization level of about 9. Its molecular weight is about 582.9 g/mol at this average level, while product labels usually list it as approximately 600. Its pharmacopoeial name is lauromacrogol 400. The nonaethylene homolog has CAS number 3055-99-0, while the wider family of polyoxyethylene lauryl ethers has CAS number 9002-92-0. Product specifications must control the distribution of chain lengths rather than a single molecular formula. Hydroxyl value, water content, free alcohol, dioxane, and residual ethylene oxide help control this distribution.

Polidocanol reaches patients in three product formats. Liquid ampoules run 0.5, 1, 2 & 3 percent in 2 mL glass, giving 10 to 60 mg per unit, with the lower strengths used on the finest vessels. The injectable foam carries 1.3 mg of the surfactant in each milliliter of foam, generated at the point of use. Topical formulations use it for its local anesthetic and antipruritic effect rather than for sclerosis. Every injectable form carries about 5 percent ethanol, which keeps the surfactant dissolved and stable. Strength, volume, vessel size, and compression regime all change together across the range.

Polidocanol formulations are simple, and the excipient list reflects that. Water for injection, ethanol, disodium hydrogen phosphate dihydrate, potassium dihydrogen phosphate & nothing else make up the liquid product. The pH sits between 6.5 and 8.0 in the American product and between 6.0 and 7.5 in the foam. Solutions are colorless to faintly greenish-yellow, preservative-free, buffered & single-use. Shelf life is three years with no special storage conditions. Ampoule glass, label stock, cartons, leaflets, and tamper features complete the finished unit.

Main End-Uses of Polidocanol

Polidocanol treats spider and reticular veins in its most common use. The 0.5 percent strength handles vessels of 1 mm or less, while the 1 percent strength handles reticular veins of 1 to 3 mm. Injections run 0.1 to 0.3 mL each, with no more than 10 mL in one session, followed by compression for two to three days on spider veins and five to seven on reticular ones. The surfactant damages the vessel endothelium, platelets gather at the injury, and a plug of platelets, debris & fibrin closes the vein. Fibrous connective tissue replaces the vessel over time. Vessel diameter, injection volume, concentration, and compression decide the result.

Polidocanol foam extends the same chemistry to truncal veins. The foam treats incompetent great saphenous veins, accessory saphenous veins, tributaries & visible varicosities above and below the knee. Gas composition is controlled at 65 parts oxygen to 35 parts carbon dioxide with nitrogen under 0.8 percent, in a liquid-to-gas ratio near one to seven. Median bubble diameter stays below 100 micrometers, with none above 500. Foam has to be injected within 75 seconds of leaving the canister, at up to 5 mL per shot and 15 mL per session. Canister pressure, bubble size, gas ratio, and transfer technique all shape foam stability.

Polidocanol also serves two older indications and one topical market. Endoscopic injection treats esophageal varices, and injection sclerotherapy treats hemorrhoids, both long established in European practice. Dermatology products use the surfactant topically against itch, often alongside urea. Laboratory and detergent grades of the same chemistry sell into entirely separate markets at a fraction of the price. Purity, documentation, sterility, endotoxin, and traceability separate those grades completely.

Polidocanol Market Risks

Polidocanol has specific quality risks because of how it is made. Ethoxylation produces 1,4-dioxane as a byproduct, and this substance is considered a possible human carcinogen. Therefore, its removal and testing are essential. Residual ethylene oxide must also be controlled for safety reasons. Detergent-grade polidocanol cannot simply be relabelled for pharmaceutical use because drug standards set much lower limits for impurities than industrial standards. This difference keeps the number of pharmaceutical suppliers small. Manufacturers must pass audits, complete regulatory filings and stability studies, validate testing methods, and undergo inspections before they can qualify.

Polidocanol also faces competition from other varicose vein treatments. These include thermal ablation, radiofrequency treatment, laser closure, cyanoacrylate glue, and mechanochemical devices. Reimbursement policies influence which treatment clinics choose, and these policies vary by country and payer. Cosmetic treatments for spider veins depend on people's willingness to spend money and may decline during an economic downturn. Clinic volumes, prices, patient financing, and seasonal demand also affect this market. Polidocanol is an old, unpatented drug, so its active ingredient faces constant price competition. Brands, delivery formats, clinical evidence, and training support help companies stand out from competitors.

Polidocanol Production Process and Main Cost Drivers

The polidocanol production process runs from lauryl alcohol and ethylene oxide through base-catalyzed ethoxylation, neutralization, stripping of volatiles, dioxane removal, filtration, assay adjustment, and sterile formulation into ampoules or canisters.

  1. By Base-Catalyzed Ethoxylation of Lauryl Alcohol with Ethylene Oxide: The main inputs are lauryl alcohol, ethylene oxide, potassium hydroxide catalyst, neutralizing acid, nitrogen, ethanol, phosphate buffer salts, water for injection, glass ampoules & packaging.

Polidocanol is built one ethylene oxide unit at a time. Lauryl alcohol and potassium hydroxide are charged, dried under vacuum, and purged with nitrogen until oxygen is gone. Ethylene oxide is then fed slowly into the reactor at around 180 degree Celsius and 1 to 2 bar, where it inserts into the alcohol oxygen bond. The reaction gives off about 92 kilojoules for every mole of ethylene oxide consumed, which is why feed rate, cooling & temperature control carry the whole safety case. A runaway in an ethoxylation reactor is the hazard every plant is designed against. Nothing is left to chance. Feed interlocks, emergency quench, relief sizing, inerting & detection all answer that risk.

Polidocanol quality is decided by the chain length distribution and by what leaves with it. The growing ethoxylate reacts more readily than the starting alcohol, so chains spread out around the mean of nine rather than sitting on it. Catalyst choice narrows that spread, and narrow-range catalysts exist for exactly this purpose. After the feed ends, the batch is held to consume free ethylene oxide, then cooled, neutralized & stripped under vacuum. Dioxane and residual oxide are removed in that stripping step, and both are measured afterward. Pharmaceutical material then goes through filtration, assay adjustment, aseptic filling into ampoules, terminal treatment where applicable & release testing. Batch size, hold times, filter ratings, and line speed are fixed in the validated process.

Main Factors Affecting Polidocanol Production Cost

Polidocanol production cost begins with two commodity inputs and ends with pharmaceutical overhead. Lauryl alcohol comes from palm kernel or coconut oleochemistry, or from petrochemical routes, and its price moves with those chains. Ethylene oxide is cheap per tonne, tightly regulated in transport & handled only by plants licensed for it. Nine moles of oxide go onto each mole of alcohol, so the oxide contributes most of the finished mass. Feedstock origin, chain cut, iodine value, and moisture all shift the alcohol price. Catalyst, neutralizing acid, filter aid & nitrogen are minor lines by comparison.

Polidocanol conversion cost is dominated neither by materials nor by labor, but by the gap between grades. Industrial ethoxylate sells by the tonne, while pharmaceutical lauromacrogol sells by the kilogram at many times the price, and the difference is testing, documentation & purification. Stripping to meet dioxane and ethylene oxide limits costs vacuum, time & yield. Sterile filling into 2 mL ampoules is slow, labor-heavy & capital-intensive relative to the volume filled. Release testing covers assay, hydroxyl value, chain distribution, residual solvents, endotoxin & sterility. A failed lot at fill writes off the batch behind it. Rejects, stoppages, media fills, requalification, and investigation time all cost suite days.

Raw Materials for Polidocanol Production Plant and its Procurement

Polidocanol production requires a small number of raw materials, which are generally inexpensive but subject to strict controls at certain stages. Lauryl alcohol is purchased in pharmaceutical or high industrial grades, with limits set for its chain length distribution and iodine value. Ethylene oxide is delivered in dedicated tankers or cylinders under strict transport rules. Potassium hydroxide, phosphoric acid or acetic acid for neutralization, nitrogen, cooling media, and filter aids are also used in the process. Formulation requires ethanol, phosphate salts, water for injection, cartons, and Type I glass ampoules.

Polidocanol plants carefully check raw materials because impurities can carry through to the final product. Lauryl alcohol batches are tested for carbon chain distribution, moisture, peroxide value, and trace metals, as these can affect the final product. Ethylene oxide purity affects both byproduct formation and production yield. Glass ampoules are tested for delamination risk, hydrolytic resistance, break force, and dimensional accuracy. Buyers keep extra stocks of lauryl alcohol and glass ampoules rather than ethylene oxide, which is usually supplied through pipelines or delivered according to production schedules. Delivery times, minimum order quantities, transport licences, and storage limits influence these purchasing decisions.

Sustainability and Regulatory Requirements

Polidocanol production must follow two sets of regulations. Ethylene oxide handling is subject to strict process safety rules, including containment, gas detection, pressure relief, and emergency planning. The finished active ingredient must meet pharmaceutical good manufacturing practice requirements, the lauromacrogol 400 monograph, and the product license. The most important quality checks cover 1,4-dioxane and residual ethylene oxide, along with assay and hydroxyl value. Aseptic filling must also follow rules for sterile manufacturing. These include environmental monitoring, media fill tests, protective clothing, staff training, and proper data management.

The environmental impact of polidocanol plants is mainly linked to ethylene oxide. Gases released from the reactor and stripper are treated using scrubbers or oxidation systems instead of being released directly, because ethylene oxide is flammable and carcinogenic. Condensate collected during stripping contains dioxane and must be handled as hazardous waste rather than sent to a general wastewater treatment plant. Energy is used for heating, vacuum generation, nitrogen supply, and cooling the heat released during the reaction. Water use is limited in most production stages, but making water for injection requires more. Main waste streams include scrubber liquid, stripped condensate, used filter aids, and rinse water.

CAPEX and OPEX for a Polidocanol Production Plant

The polidocanol plant setup cost is divided between a hazardous reaction block and a sterile filling suite. Ethoxylation needs a jacketed pressure reactor with high cooling capacity, oxide metering, nitrogen inerting, emergency quench & interlocked controls. Downstream equipment covers neutralization, vacuum stripping, filtration, intermediate storage & drumming. The pharmaceutical side needs water for injection generation, compounding vessels, sterile filtration, ampoule washing and filling lines, inspection & packaging. Quality control needs chromatography for chain distribution, headspace analysis for oxide and dioxane, endotoxin testing & sterility capability. Qualification runs through design, installation, operation, performance & cleaning validation.

Polidocanol operating costs are relatively low for raw materials but high for regulatory compliance. Lauryl alcohol and ethylene oxide account for a modest share of costs compared with the selling price of pharmaceutical-grade polidocanol. Labor costs cover reactor operators, sterile filling staff, quality control analysts, engineers, and regulatory staff. Utilities include steam, cooling water, vacuum, nitrogen, clean steam, and water for injection. Ampoules, cartons, and leaflets add to the packaging cost of each 2 mL unit. Depreciation costs are higher for the filling area than for the reactor because sterile production requires expensive validation. Sterile filling capacity is the main factor affecting production costs. Insurance, calibration, maintenance, monitoring, and waste disposal add to fixed costs.

Plant Location and Investment Factors

Polidocanol plants follow ethylene oxide access and pharmaceutical infrastructure. A site inside a chemical park with piped oxide avoids the hardest part of the supply chain, since shipping the gas is restricted and expensive. Germany holds the originator operation at Wiesbaden, with decades of process history behind it. India and China host active ingredient capacity at lower cost, close to surfactant chemistry. Filling and packaging are often placed near the selling market rather than near the reactor. Permits, oxide access, skilled operators, inspection history & logistics decide the site.

Polidocanol investment decisions turn on which part of the chain to occupy. Making industrial ethoxylate is a commodity business with thin margins and large volumes. Making pharmaceutical lauromacrogol means small volumes, heavy documentation, slow qualification & far better margins. Buying active ingredient and filling ampoules is a third model, and it suits companies with sterile capacity but no oxide license. Foam products add a device element, since the canister and transfer unit matter as much as the solution. Canister supply, valve quality, assembly, and sterilization all enter that business case.

Major Polidocanol Producing Regions

Polidocanol production centers on Germany, with supporting capacity in Asia and the United States. Wiesbaden holds the originator plant, where Kreussler has made the European reference product for decades. Switzerland and Germany together supply much of the pharmacy and compounding trade through established distributors. India and China provide active ingredient and intermediate supply, with exporters in Bangalore and Jiangsu both appearing in the trade. The United States hosts foam manufacturing and American market supply. Surfactant-grade material of the same chemistry is made across every major chemical region. Europe, North America, India, China, and Southeast Asia all host ethoxylation capacity.

Key Polidocanol Producers

Chemische Fabrik Kreussler

  • German pharmaceutical company based in Wiesbaden, holding the original product license.
  • Markets the sclerosant as Aethoxysklerol at 0.5, 1, 2 & 3 percent in 2 mL ampoules.
  • Competes on originator status, decades of clinical use, formulation know-how & European reach.
  • Holds authorizations first granted in 1971 and renewed since.

Merz Pharmaceuticals

  • German pharmaceutical group with an aesthetics and dermatology franchise.
  • Supplies the American market with 0.5 and 1 percent ampoules under the Asclera name.
  • Competes on aesthetic channel access, physician training, brand recognition & distribution.
  • Fills single-use preservative-free ampoules buffered between pH 6.5 and 8.0.

Boston Scientific

  • American medical device group supplying the injectable foam presentation.
  • Delivers 1.3 mg of the surfactant per milliliter of foam from a two-canister system.
  • Competes on the device, controlled bubble size, ultrasound-guided technique & vein clinic reach.
  • Controls the gas at 65 parts oxygen to 35 parts carbon dioxide with nitrogen under 0.8 percent.

Agno Pharma

  • Active ingredient producer with operations in the United States and Jiangsu.
  • Supplies polidocanol active ingredient and reference standard material to formulators.
  • Competes on regulatory filing coverage, documentation, small lot supply & export experience.
  • Holds a United States drug master file for the active ingredient.

Maiva Pharma

  • Indian pharmaceutical company based in Bangalore serving injectable markets.
  • Appears in the polidocanol trade as an exporter of active ingredient quantities.
  • Competes on Indian cost base, injectable capability, flexibility & export reach.
  • Supplies development and analytical quantities alongside commercial material.

Hänseler

  • Swiss supplier of pharmacy raw materials and compounding ingredients.
  • Distributes polidocanol of Swiss origin under good manufacturing practice documentation.
  • Competes on pharmacy channel reach, documentation quality, small pack sizes & reliability.
  • Serves compounding pharmacies rather than industrial formulators.

Polidocanol Production Cost Report

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Product Details

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Product Details

Particulars Details
Product Name Polidocanol
Scope Production Process: Process Flow, Material Flow, Material Balance

Raw Material and Product Specifications: Raw Material Consumption, Product and Co-product Generation

Land and Site Cost: Offsites/Civil Works, Equipment Cost, Auxiliary Equipment Costs, Contingency, Engineering and Consulting Charges, Working Capital

Variable Cost: Raw Material, Utilities, Other Variable Costs

Fixed Cost: Labor Requirements and Wages, Overhead Expenses, Maintenance Charges, Other Fixed Costs

Financing Costs: Interest on Working Capital, Interest on Loans

Other Costs: Depreciation Charges, General Sales and Admin Cost
Currency US$ (Data can also be provided in the local currency)
Customization Scope The report can be customized as per the requirement of the customer
Post-Sale Analysts Report 10-12 weeks of post-purchase analyst support after report delivery for any queries from the deliverable
Delivery Format PDF and Excel format through email (editable version in PPT/Word format of the report can be also provided on special request)

Frequently Asked Questions

A bunded lauryl alcohol store, an ethylene oxide receiving and metering system with gas detection and emergency isolation, a jacketed pressure reactor with high cooling capacity and interlocked controls, neutralization and vacuum stripping equipment, filtration and intermediate storage, scrubbing or thermal oxidation on all vents, a water for injection plant, compounding and sterile filtration skids, ampoule washing and filling lines with inspection, and laboratories running chromatography, headspace analysis, endotoxin and sterility testing.
Lauryl alcohol is charged with potassium hydroxide, dried under vacuum and purged with nitrogen. Ethylene oxide is metered in at about 180 degree Celsius and 1 to 2 bar until roughly nine units have added on average, then the batch is held to consume free oxide. Neutralization, vacuum stripping of oxide and 1,4-dioxane, and filtration give the active ingredient, which is compounded with ethanol and phosphate buffer in water for injection and filled into ampoules.
Lauryl alcohol from oleochemical or petrochemical sources, ethylene oxide at roughly nine moles per mole of alcohol, potassium hydroxide catalyst, neutralizing acid, nitrogen, and filter aids, with ethanol, phosphate salts, water for injection and type I glass on the formulation side. Ethylene oxide contributes most of the finished mass, while the alcohol sets the chain that defines the molecule.
A pressure-rated ethoxylation reactor with jacket cooling, oxide metering and nitrogen inerting, vacuum stripping capability, neutralization vessels, filtration, drumming or bulk storage, and on the sterile side a water for injection still, compounding tanks, sterile filtration, ampoule washing, filling and sealing lines and automated inspection. Utilities cover steam, cooling water, chilled water, vacuum, nitrogen, clean steam, compressed air, and vent scrubbing.
Lauryl alcohol and ethylene oxide prices, oxide addition rate against reactor cooling capacity, chain distribution control and catalyst choice, stripping efficiency for dioxane and residual oxide, batch size against the small pharmaceutical demand, sterile fill line speed and reject rate, analytical release testing, ampoule and packaging cost, and the compliance burden of running ethylene oxide chemistry.
The active ingredient is made under pharmaceutical good manufacturing practice against the lauromacrogol 400 monograph, with limits on 1,4-dioxane and residual ethylene oxide as the defining tests alongside assay and hydroxyl value. Finished injectables follow the sterile manufacturing annex, with endotoxin and sterility release testing. Ethylene oxide handling falls under process safety and major hazard regulation in parallel with the pharmaceutical rules.
Germany holds the originator position, where Kreussler makes the European reference product at Wiesbaden and Merz supplies the American market under its own brand. Boston Scientific manufactures the foam presentation for the United States. India and China supply active ingredient through companies such as Maiva Pharma and Agno Pharma, and Swiss and German distributors serve the pharmacy trade.
The same ethoxylation makes both grades, yet pharmaceutical material carries dioxane and ethylene oxide limits, documentation and sterility requirements that industrial surfactant never faces. That testing and purification burden, not the chemistry, explains the price gap between a tonne of detergent ethoxylate and a kilogram of lauromacrogol. It also keeps the qualified pharmaceutical supply base small, since few ethoxylation plants carry pharmaceutical systems.
Pharmaceutical active ingredient to the lauromacrogol 400 monograph, finished injectable solutions at 0.5, 1, 2 and 3 percent in 2 mL ampoules, injectable foam at 1.3 mg per milliliter of foam, and topical grades for anti-itch dermatology products. Industrial and laboratory surfactant grades of the same chemistry are sold separately at far lower prices and cannot be used in medicines.
Narrow-range catalysts replace conventional potassium hydroxide to tighten the chain distribution around the mean, which cuts both free alcohol and long-chain homologs. Continuous or loop ethoxylation reactors substitute for batch operation, improving heat removal and shortening cycle time at higher capital cost. The chemistry itself does not change, since adding ethylene oxide to lauryl alcohol is the only practical route to this molecule.
Ethylene oxide, counted with the infrastructure its use demands. It supplies most of the finished mass, and the licensing, containment, detection and emergency systems around it set both the capital cost and the short list of plants able to make the molecule at all.

How does our Polidocanol Production Cost Report Provide Exhaustive Data and Extensive Insights?

At Procurement Resource, we focus on improving the should-cost of production for polidocanol and map every stage of the route, from lauryl alcohol and ethylene oxide receipt through catalyst charging with potassium hydroxide, vacuum drying of the alcohol charge, nitrogen purging to remove oxygen, controlled ethylene oxide addition at around 180 degree Celsius and 1 to 2 bar with full exotherm management, the hold period that consumes free oxide, cooling and neutralization of the catalyst, vacuum stripping of residual ethylene oxide and 1,4-dioxane, filtration, assay and hydroxyl value adjustment, compounding with ethanol and phosphate buffer in water for injection, sterile filtration, ampoule washing and filling, inspection, and release testing. The cost model resolves each input separately, including lauryl alcohol, ethylene oxide, potassium hydroxide, neutralizing acid, nitrogen, filter aids, ethanol, phosphate salts, water for injection, type I glass ampoules, cartons and leaflets, steam, vacuum and cooling duty, scrubbing and waste treatment, labor across the reaction and sterile areas, and analytical release testing. We evaluate CAPEX and OPEX as cost per kilogram of active ingredient and per filled ampoule, isolating the ethoxylation share, the purification and testing share, and the sterile filling share, since these items set most of the delivered cost.

Alongside the cost build-up, the report identifies technology providers for ethoxylation reactors and oxide metering systems, vacuum stripping columns, scrubbers and thermal oxidizers, water for injection generation, compounding and sterile filtration skids, ampoule washing and filling lines, and inspection equipment, and offers a supplier database for lauryl alcohol, ethylene oxide, catalysts, pharmaceutical excipients, and type I glass. It sets out a feasible plant layout covering a bunded alcohol store, an ethylene oxide receiving and metering area with full detection, the reaction block behind protection, neutralization and stripping, intermediate storage, a water for injection plant, compounding and sterile filling suites, inspection and packing, scrubbing and waste treatment, and quality control laboratories. By modeling oxide addition rate, chain distribution, stripping efficiency, fill line speed, and batch success rate, the analysis shows where the cash production cost can be reduced. It supports decisions on industrial against pharmaceutical grade, conventional against narrow-range catalysis, in-house active ingredient against purchase, and liquid ampoule against foam presentation.

About the Author

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Vishakha Agrawal

Lead - Social & Development Research

Delivering procurement intelligence and supply chain analytics across healthcare, FMCG, and chemicals sectors, with expertise in cost modeling, vendor mapping, and spend optimization to support data-driven sourcing decisions and procurement outcomes.

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