
Udeesha Tomar
AVP - Strategy and Solutions
Leading procurement research solutions across chemicals, materials, and food & beverages, with expertise in price forecasting and market analytics.
The report provides detailed analysis essential for establishing an ethyl hexanoate production plant. It encompasses all critical aspects necessary for ethyl hexanoate production, including the cost of ethyl hexanoate production, ethyl hexanoate plant cost, ethyl hexanoate production costs, and the overall ethyl hexanoate production plant cost. Additionally, the study covers specific expenditures associated with setting up and operating an ethyl hexanoate 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.
Ethyl hexanoate is a chemical used in the flavor, fragrance, food, and beverage industries. It is also called ethyl caproate and is supplied for making food flavors, perfumes, and other specialty products. It is available in natural and synthetic grades for flavor production and laboratory testing. Buyers choose the grade based on its intended use, quality needs, and supplier specifications. Demand depends on the production of food flavorings, beverages, perfumes, and other products that use flavor and fragrance ingredients.
Ethyl hexanoate is available in natural and synthetic grades. Specialist aroma suppliers in Germany, the United States, and the United Kingdom offer natural grades, often with kosher certification. Synthetic grades mainly come from Chinese chemical plants, which offer 99% purity and supply several tonnes at a time. Buyers check the manufacturing site, product grade, certifications, packaging, and delivery time before placing orders. Certification requirements may include food safety compliance, kosher status, proof of origin, and traceability records. Some Chinese suppliers also accept orders starting at one kilogram.
Ethyl hexanoate demand mainly comes from the fruit flavor industry. It is used in flavor formulations for beverages, confectionery, and other food products. An ethyl hexanoate demand and supply analysis considers beverage production, confectionery launches, the price difference between natural and synthetic grades, use in perfumes, and the cost of hexanoic acid. Demand also depends on flavor house formulations and seasonal product requirements. Flavor manufacturers consider the amount needed, aroma strength, stability, and cost when choosing a grade. Since the compound can be detected at very low concentrations, small quantities can be used in large volumes of products. Buyers may purchase both grades, using synthetic material to reduce costs and natural material when product labeling requires it.
Ethyl hexanoate is a clear, colorless liquid. It melts at minus 67 degree Celsius and boils between 167 and 168 degree Celsius. Its density is 0.871 grams per milliliter at 20 degree Celsius, and its refractive index ranges from 1.407 to 1.41. Its reported partition coefficient is 2.96. Quality checks cover these properties, along with flash point and solubility. Safe handling depends on its flammability, exposure to light, temperature, container type, and transport time. Product documents include specifications, testing methods, batch records, certificates of analysis, safety data sheets, and labels.
Ethyl hexanoate is first graded by purity. One supplier specifies a minimum purity of 99.0% by gas chromatography; other catalog grades offer 99% or higher, and natural grades are available at a minimum of 98%. These differences may result from the amount of unreacted acid and related ester impurities present. Quality testing covers identity, purity, acid value, refractive index, and odor. Product specifications define purity limits, impurity levels, color, odor, and required documents. The levels of unreacted acid and related ester impurities help distinguish a 98% grade from a 99% grade.
Ethyl hexanoate is also graded by its source. Natural grade is made from natural raw materials and sold at a higher price, often with food compliance and kosher certification. Synthetic grade contains the same compound and serves similar applications, but is generally sold at a different price. Both grades may be listed under the names ethyl hexanoate and ethyl caproate. Origin records include the raw material source, supplier declarations, certificates of analysis, traceability documents, and audit records. Natural-grade material may require kosher certificates, food compliance documents, and proof of its natural status in Europe. Both grades contain the same compound, but their prices vary depending on the production method and raw materials used. Audits include site inspections, document checks, material tracking, supply chain reviews, sample testing, and certification renewals.
Ethyl hexanoate is mainly used to make fruit flavors for beverages, confectionery, and other food products. It helps create fruit flavors with pineapple notes and hints of banana and strawberry. Only small amounts are needed because it can be detected at very low concentrations. Flavor manufacturers consider the type of product, amount used, effect on the final flavor, labeling requirements, and shelf life. Common uses include pineapple, apple, strawberry, banana, and tropical fruit flavors. Production records track the product type, amount used, batch details, flavor quality, shelf life, and sensory test results.
Ethyl hexanoate is also used in fragrances, mainly in small amounts to add fruity and floral notes. Perfumers use it to give a fragrance a fresh, fruity opening rather than to create its main scent. Larger quantities are generally used in fruit flavor formulations. Fragrance manufacturers consider dosage, blending ingredients, evaporation rate, stability, and cost. Perfumers also assess how the ingredient interacts with other fragrance notes and whether it meets applicable regulations. Product development records cover its role in the fragrance, dosage, stability, color changes, and cost of use.
Ethyl hexanoate is also found naturally in several fruits and beverages. It is found in strawberry, apple, pineapple, guava, kiwi, and blackcurrant, as well as cocoa, rum, bourbon, and grape wines. It is also identified as a flavor component of baijiu, a traditional Chinese spirit. Its presence in these natural sources supports demand for natural-grade ethyl hexanoate. Market assessments consider its occurrence in fruits, spirits, fermented beverages, cocoa, and grape wines when evaluating natural-grade products.
Ethyl hexanoate production costs depend mainly on hexanoic acid, also called caproic acid. This acid provides six of the eight carbon atoms in the compound, so changes in its price directly affect production costs. Natural-grade ethyl hexanoate faces higher cost risks because natural raw materials are less available and more expensive than those used in synthetic production. Cost planning considers caproic acid prices, the availability of natural raw materials, ethanol costs, and freight charges. Buyers and producers compare the prices of natural and synthetic grades, secure supply contracts, and maintain enough stock to avoid supply problems. Natural-grade production can be much more expensive because it uses costlier raw materials to obtain the same six carbon atoms.
Ethyl hexanoate also has safety and handling risks. It is a flammable liquid transported under Class 3, Packing Group III. However, suppliers report different hazard information. One supplier lists only flammability, while another also reports risks to the skin, eyes, and aquatic life. These differences can make product labeling more difficult for buyers. Safety checks cover signal words, hazard statements, transport class, packing group, and labeling requirements. Buyers compare supplier safety data sheets with their own risk assessments, product labels, and workplace safety rules. Flammable liquid storage requirements apply to all grades. Even a six-degree difference in reported flash points can affect the storage rules that need to be followed.
The ethyl hexanoate production process runs from hexanoic acid and ethanol over an acid catalyst, with water removed to drive the equilibrium.
Ethyl hexanoate is produced by reacting caproic acid with ethanol in the presence of an acid catalyst, such as concentrated sulfuric acid or hydrochloric acid. Extra ethanol is used to help the reaction proceed, and the water formed during the reaction is removed to increase the yield. The reaction process requires control of the acid quantity, excess ethanol, catalyst amount, reflux rate, and water removal. Operators monitor the batch temperature, amount of water collected, acid value, and reflux conditions. If water is no longer removed, the reaction may stop progressing toward higher conversion.
After the reaction, ethyl hexanoate is purified through neutralization and distillation. The catalyst is neutralized, and the crude product is washed to remove salts and remaining acid. Excess ethanol is recovered for reuse. Fractional distillation then separates the ester near its boiling point of 168 degree Celsius. The main product fraction is checked for both odor and purity. Work-up controls include quenching, neutralization pH, washing, phase separation, and drying. Distillation requires control of column stages, reflux ratio, early fractions, the main product fraction, and remaining residue. Final checks assess the odor and chromatographic purity of the product.
Ethyl hexanoate production costs depend mainly on hexanoic acid, which makes up most of the raw material cost. Ethanol, sulfuric acid, and water cost less than the acid. Natural-grade production costs several times more because it uses more expensive raw materials. Cost calculations include hexanoic acid, ethanol, catalysts, neutralizing agents, utilities, testing, packaging, and waste disposal. Each batch also requires time for adding materials, running the reaction, neutralizing, washing, distilling, and cleaning the equipment. Ethanol and sulfuric acid are commonly available industrial materials, while hexanoic acid is the main specialty raw material. Batch records track the quantities of materials used, reactant ratios, temperature, reaction time, water collected, and final product yield.
Ethyl hexanoate conversion costs mainly depend on removing water and achieving the required product quality. Water must be removed during the reaction to improve conversion, so methods such as azeotropic distillation or adding extra ethanol are used. During final distillation, the equipment must separate esters with similar boiling points while maintaining the desired aroma. Column design depends on the number of stages, packing type, reflux rate, condenser capacity, and use of vacuum. Aroma quality also depends on heating time, contact with metal surfaces, exposure to light, and nitrogen blanketing. Esters with similar boiling points are harder to separate, which affects the number of stages needed in the distillation column. The remaining liquid may still contain useful ethyl hexanoate, which can be recovered through another distillation cycle.
Ethyl hexanoate production mainly requires two raw materials: hexanoic acid and ethanol. Both are purchased based on their purity, moisture content, color, and odor. Plants making natural-grade ethyl hexanoate also need documents confirming the origin of these materials. The quality and smell of hexanoic acid strongly affect the smell of the final product. Incoming quality checks cover purity, moisture, acid value, color, and odor. Purchase contracts specify the quantity, price, delivery dates, retesting dates, and required documents. Supplier approval includes site audits, sample batches, agreed purity levels, odor checks, origin verification, and document reviews.
Ethyl hexanoate plants also need other materials for production and packaging. Concentrated sulfuric acid or hydrochloric acid is used as a catalyst, while sodium carbonate or caustic soda is used for neutralization. A suitable solvent may be used to help remove water during the reaction. Other supplies include drums, closures, nitrogen, and packaging that protects the product from light. Purchasing covers acid catalysts, bases, water-removal solvents, drying agents, and packaging materials. Acids, alcohols, catalysts, solvents, drums, and closures are stored under separate controls. Flammable liquid safety measures apply to the ethanol storage area as well as the finished product tanks.
Ethyl hexanoate is regulated for use as a flavoring substance and fragrance ingredient. It has an American flavor number and a number assigned by the Joint FAO/WHO Expert Committee on Food Additives. It is listed on the US chemical inventory and registered in Europe. Its harmonized code is 29159000, and Germany classifies it under water hazard class 1, the lowest of the three classes. Compliance checks cover flavor listings, chemical inventory status, safety data sheets, and customer declarations. Safety information includes flammability, skin and eye irritation, effects on aquatic life, and safe handling requirements. Water hazard class 1 indicates the lowest level of water hazard under the German classification system.
Ethyl hexanoate has a relatively low environmental impact because it breaks down easily, and published data show low acute toxicity. Reported oral toxicity in rats and skin toxicity in rabbits are both above 5 grams per kilogram. Waste from production includes used acid liquid, wash water, recovered alcohol, and distillation residue. Flammable liquid storage rules apply to the storage area. Waste management covers used acid, wash water, distillation residue, and solvent vapors. Plants aim to recover excess ethanol, solvents used for water removal, condensed vapors, and heat from the distillation column. Distillation residue is the main source of organic waste during production. Environmental monitoring tracks vapor emissions, wastewater levels, solvent recovery, waste residue volumes, disposal records, and water use.
The ethyl hexanoate plant setup cost includes the cost of a stainless steel or glass-lined reactor with a reflux system and water separator. It also requires vessels for neutralization and washing, equipment for separating liquids, an alcohol recovery column, and a fractionating column that can separate esters with similar boiling points. Capital costs cover reactors, separator heads, washing vessels, separation equipment, columns, condensers, and storage tanks. The filling area also needs weighing equipment, drum handling systems, nitrogen blanketing, labeling facilities, and warehouse space. The height and capacity of the distillation column, rather than the reactor size, mainly determine the equipment needed for final purification.
Ethyl hexanoate operating costs mainly include hexanoic acid, ethanol, catalyst, and energy for distillation. Hexanoic acid accounts for the largest share of the cost, followed by steam and energy used in the fractionating column. Quality testing includes gas chromatography to check purity, acid value, refractive index, specific gravity, color, and smell. Operating costs cover raw materials, alcohol, catalyst, utilities, labor, testing, packaging, and freight. Fixed costs include salaries, maintenance, insurance, registrations, depreciation, and quality system maintenance. Sensory testing adds to the cost because the product's smell and flavor must meet the required standards before release. Overheads include utilities, maintenance, equipment calibration, environmental monitoring, waste disposal, and audit preparation.
Ethyl hexanoate production depends on the supply of hexanoic acid and access to flavor markets. Chinese plants dominate synthetic-grade supply because of their lower costs, while specialist suppliers in Germany, the United States, and the United Kingdom focus on natural-grade material. Distributors in Switzerland and the United States also supply the market. Site selection considers raw material availability, alcohol transport, distillation facilities, skilled labor, and wastewater treatment capacity. Producers tend to operate near existing ester manufacturing facilities rather than close to flavor markets. For natural-grade production, certification requirements and access to audits are more important than low production costs. Logistics planning covers acid imports, alcohol supply, drum availability, port access, flammable liquid storage and delivery terms.
Investment decisions for ethyl hexanoate depend mainly on the grade being produced. Synthetic-grade producers compete with established Chinese suppliers on price, while natural-grade producers compete through certification, documentation, and traceability and can charge much higher prices. Ethyl hexanoate is usually produced in batches using shared equipment at a multipurpose ester plant. Investment decisions consider the product grade, batch duration, certification requirements, customer mix, and shared production capacity. Returns depend on raw material prices, conversion rates, distillation recovery, odor quality, and selling price. The higher price of natural-grade material can support a smaller production facility. However, certification renewals and audit costs are greater concerns for natural-grade producers than for synthetic-grade suppliers.
Ethyl hexanoate production is divided between synthetic manufacturers in China and natural-grade suppliers in Western countries. Chinese suppliers are located mainly in Hebei, Shandong, Shaanxi, and Henan, where they offer large quantities and short delivery times. Natural-grade material is supplied by companies in Germany, the United States, and the United Kingdom, often with kosher and food compliance certificates. Distributors in Switzerland and the United States supply both grades to the flavor industry. Regional strengths depend on access to hexanoic acid, ester production facilities, certification, documentation, and customer markets. Supplier listings include manufacturers, natural-grade specialists, catalog suppliers, and flavor distributors. Chinese producers mainly supply Western companies that prepare flavor blends, while Western specialist suppliers provide natural-grade material for these formulations. Trade records cover product origin, certificates of analysis, customs classification, storage conditions, transit time, and delivery terms.
Axxence Aromatic
Advanced Biotech
Alfrebro
Augustus Oils
Tokyo Chemical Industry
Hebei Chuanghai Biotechnology
Ethyl Hexanoate Production Cost Report

Choose What's Right for You
Pay Via

| Particulars | Details |
|---|---|
| Product Name | Ethyl Hexanoate |
| 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) |
Ethyl Hexanoate Production Cost Processes with Cost Analysis

This study analyzes Ethyl Hexanoate Production by Esterification of Caproic Acid with Ethanol in Acidic Medium, covering manufacturing, process flow, operating expenses, and financial considerations.
At Procurement Resource, we focus on improving the should-cost of production for ethyl hexanoate and map every stage of the route, from receipt and assay of hexanoic acid and ethanol against assay, moisture, color and odor, with origin documentation where a natural grade is being made, through charging of the acid with a molar excess of ethanol and a catalytic charge of concentrated sulfuric or hydrochloric acid into a reactor fitted with a reflux head and a water separator, heating to reflux with continuous removal of the water of reaction as an azeotrope over several hours with conversion followed by acid value, cooling and quenching of the catalyst, neutralization with aqueous sodium carbonate or caustic to a defined pH, washing with water to remove salts and residual acid, phase separation and drying of the crude ester, recovery of the excess alcohol and any azeotroping solvent by atmospheric distillation for reuse, fractional distillation of the crude through a packed or trayed column with a forerun cut, a heart cut taken near 168 degree Celsius and a residue cut, gas chromatographic and sensory evaluation of the heart cut, blending to the assay specification, and filling into drums under nitrogen with light protection. The cost model resolves each input separately, including hexanoic acid at both synthetic and natural price points, ethanol, acid catalyst, neutralizing agents, azeotroping solvent with recovery losses, drying agents, process water, nitrogen, steam, cooling water, vacuum where used, electricity for pumping, agitation and distillation reflux, drums, closures and labels, laboratory testing for assay, acid value, refractive index, specific gravity, color and sensory profile, stability and shelf life work, flavor and fragrance regulatory maintenance including kosher and food compliance documentation where claimed, waste handling for spent acid, aqueous washes and distillation residues, labor across charging, reaction, work up, distillation and filling, and freight. We evaluate CAPEX and OPEX as cost per kilogram of finished ester, isolating the hexanoic acid share, the catalyst and alcohol share, and the distillation energy share, since these items set most of the delivered cost.
Alongside the cost build-up, the report identifies technology providers for stainless and glass lined reactors with reflux and water separator heads, dosing skids for catalyst addition, neutralization and washing vessels, coalescers and phase separation equipment, alcohol recovery columns, packed and trayed fractionating columns with reflux control and high efficiency internals, thin film evaporators for color sensitive residues, nitrogen blanketing systems, drum filling and weighing lines, and analytical instruments for gas chromatography, refractometry, color measurement and sensory evaluation, and offers a supplier database for hexanoic acid in both synthetic and natural grades, ethanol, acid catalysts and packaging. It sets out a feasible plant layout covering a raw material store with drum handling and a flammable store, a reaction hall, a neutralization and washing block, an alcohol recovery section, a fractionation section, a finished product tank farm under nitrogen, a drum filling hall, aqueous effluent handling, and a quality control laboratory with sensory booths. By modeling hexanoic acid pricing across grades, alcohol excess, catalyst loading, water removal efficiency, reaction time, column plate count, reflux ratio, cut points and odor retention, the analysis shows where the cash production cost can be reduced. It supports decisions on synthetic against natural grade, sulfuric against hydrochloric catalysis, batch against continuous water removal, and site location across Chinese, European or American capability.

AVP - Strategy and Solutions
Leading procurement research solutions across chemicals, materials, and food & beverages, with expertise in price forecasting and market analytics.
Need more help?

Still Need Help?
Compare & Choose the Right Report Version for You
How to Order Your Report?