300L Perfume Making Machine with Chilling Freezing Filtration & Pneumatic Agitator for Eau de Toilette, Cologne & Essential Oil Processing

Who the 300L Perfume Making Machine Suits

This model is intended for manufacturers who need a defined chilling and filtration stage for compatible fragrance batches. Its role is to prepare an already formulated blend for the next operation, not to replace fragrance development or establish a universal perfume-production recipe.

It is most relevant when the factory has identified a clarity requirement that can be assessed through low-temperature treatment and filtration. Eau de toilette, cologne and other fragrance products should be evaluated using their actual composition and quality targets.

A production trial should answer a clear question: what material is being removed, under which conditions, and what finished-product checks establish an acceptable result?

Distinguish This Model from a Perfume Mixing and Aging Tank

The 200L sealed pneumatic perfume mixing tank is a specific adjacent configuration for closed mixing and aging. Its confirmed scope does not include refrigeration or filtration.

These machines address different production stages. Select the required functions before comparing capacity or price; a mixing tank is not automatically a substitute for a chilling and filtration package.

Define the Purpose of Chilling Before Selecting the Process

Low-temperature treatment should serve an identified formulation requirement. Depending on the product, the intended objective may involve separating material that becomes insoluble under selected conditions before filtering it from the batch.

Confirm that the separated material is something the formulation developer intends to remove. This is particularly important when extending a perfume process to essential oils or other aromatic products.

Do not assume that chilling improves every fragrance or that one temperature applies to all alcohol, water and fragrance ratios. The approved process must balance clarification with the required product characteristics.

Set Cooling Acceptance Conditions Around the Actual Batch

The supplied range is −5°C to −10°C. Agree where temperature is measured, the starting condition, batch quantity and ambient conditions used for evaluation.

A no-load refrigeration indication is not the same as a demonstrated product temperature in a 300L batch. Likewise, reaching a temperature does not establish that the product has completed the required holding or clarification stage.

Define the required product condition and sampling method before measuring cycle time. This gives a more useful purchasing basis than an unsupported promise of rapid freezing.

Use Pneumatic Agitation for the Required Liquid-Mixing Duty

The confirmed agitator is a propeller driven by an air motor. There is no electric high-speed disperser, and the previously listed 0–1400 rpm range is not confirmed.

Obtain the delivered air-motor and shaft specifications, including the permitted operating conditions and any method provided for speed adjustment or indication.

Agitation should distribute the liquid without accepting unnecessary surface disturbance, splashing or air incorporation. The appropriate setting may differ between initial mixing, chilling and a holding stage.

Include air demand in the installation review. Operating the agitator and diaphragm pump together may require a different supply assessment from running either component alone.

Select the Final Filter Using Product Evidence

The first stage is specified as 1.0 μm. The second stage is selected as 0.45 μm or 0.22 μm, not both in an assumed three-stage sequence.

Obtain the cartridge media, dimensions, retention classification, seal materials and operating limits. A pore-size figure alone does not identify chemical compatibility, usable filtration area or expected flow.

Evaluate the finished product using the selected filter. Depending on the formulation and media, the assessment may need to include appearance, fragrance character and other agreed quality properties.

Do not present the finer option as an automatic upgrade or describe the package as sterilizing equipment without a separately supported process.

Keep Aging, Chilling and Filtration as Distinct Stages

The supplied 24–48 hour aging figure should not become a universal instruction. Define whether the product requires maturation before chilling, a cold hold before filtration, or another sequence.

Record the formulation, preparation history, temperature and holding conditions when comparing trials. Otherwise, differences observed after filtration may reflect earlier processing rather than the filter itself.

The related guide to fragrance and sensitive-ingredient addition provides broader context on treating ingredient sequence and exposure conditions as part of the process.

Review the Diaphragm Pump and Filters as One Circuit

The supplied transfer arrangement is an air-operated diaphragm pump, with ARO identified as a brand option. Confirm the actual model, wetted materials and elastomer selections in the purchase schedule.

Assess the pump together with the filter elements, housings and connecting route. Compressed-air supply pressure does not establish an approved product pressure for every component.

The pump selection guide for cosmetic, food and pharmaceutical processing provides a broader selection framework. The final duty must still be matched to the fragrance, operating temperature and filter limits.

Agree how operators identify filter loading and when processing should stop for inspection or element replacement. Do not assume unlimited flow through progressively loaded filters.

Confirm the Complete Product-Contact Material Schedule

SUS316L is specified for product-contact construction, while the cooling arrangement separately identifies a titanium coil. Confirm the coil location and the complete wetted-material schedule from the final drawing.

Include pump diaphragms, check components, filter media, housing seals, hoses and receiving connections in the compatibility review. A stainless steel vessel does not establish compatibility of every non-metallic component.

For products containing alcohol or concentrated fragrance ingredients, evaluate the actual composition and exposure conditions rather than relying on a general perfume-compatible description.

Connect Clarification with the Selected Bottling Method

The filtered batch needs a defined receiving and filling route. A clean batch can be affected by an unsuitable holding vessel, transfer hose or downstream handling method.

The semi-automatic 10-head rotary vacuum perfume filler is a specific downstream option to assess against the bottle, product and required output.

Closure selection then follows the actual package. A semi-automatic perfume bottle crimping machine serves compatible crimp-pump closures, while a perfume bottle collar pressing machine addresses a different packaging operation.

These references identify equipment stages, not proof of a matched line. Confirm bottle samples, closure geometry and the actual integration scope.

Include Filter Changeover and Residue Control in Cleaning Planning

Review access to the vessel, coil region, agitator, pump and filter housings. Confirm whether each filter element is single-use or reusable according to its own instructions.

Different fragrance products may require particular attention to retained scent and residue. Define changeover checks rather than assuming a visually clear rinse establishes acceptable cleaning.

The guide to cleaning dead corners in process equipment provides useful inspection context. No automatic CIP or validated cleaning cycle is established by the supplied specification.

Calculate Output from the Complete Clarification Cycle

The 300L batch reference is not an hourly output rating. Include charging, chilling, any required hold, filtration, recovery and cleaning when planning production.

Filter replacement frequency and compressed-air availability can affect scheduling alongside refrigeration performance. If the same vessel is also used for extended maturation, that occupancy must be included.

The machinery total cost of ownership guide provides a framework for comparing consumables, utilities, operator time and service requirements alongside the purchase price.

Prepare a Model-Specific Purchase Checklist

• Provide the fragrance composition and relevant material-handling information.
• Define the purpose and acceptance criteria for low-temperature treatment.
• Confirm routine batch quantity and the smallest batch requiring assessment.
• Agree cooling-test conditions and the required product-temperature measurement.
• Obtain the pneumatic agitator specification without assuming an unverified speed range.
• Select the final filter as 0.45 μm or 0.22 μm after the 1.0 μm stage.
• Confirm filter media, retention classification and wetted-material compatibility.
• Specify the diaphragm-pump model and operating limits.
• Review the explosion-proof supply scope against the actual site requirements.
• Define receiving, filling, cleaning and filter-changeover arrangements.
• Agree representative-product trials and the required finished-quality checks.

StriversMachinery manufactures core equipment in-house and sources complementary equipment from long-term partner manufacturers, taking responsibility for complete production line integration and delivery. For this model, the agreed scope should connect perfume clarification with product-compatible transfer, receiving and bottling operations.