100 LITERS Hydraulic Lift Vacuum Emulsifying Machine for Cream, Lotion & Cosmetic Production

Who the 100L Hydraulic Lift Vacuum Emulsifying Machine Is For

The 100L hydraulic lift vacuum emulsifying machine is intended for manufacturers who need a defined batch platform for creams, lotions, and related cosmetic formulations. Its main vessel combines a 100L working capacity with separate bulk agitation, wall scraping, bottom-entry homogenization, thermal processing, and vacuum functions.

This configuration is worth evaluating when the production requirement includes more than simple liquid blending. A formulation may need separate phase preparation, controlled heating and cooling, high-shear emulsification, and air removal within the same batch process. The integrated oil and water pots support that arrangement without establishing a single mandatory recipe sequence.

The hydraulic head also gives this model a specific operational character. It suits buyers who value open-vessel access and can provide the required lifting envelope. Selection should therefore consider how the equipment will be used and accessed between batches, alongside the product it must process. The Hydraulic Lifting Vacuum Emulsifying Mixer category provides a broader comparison of access and installation considerations.

Plan Around 100L Working Capacity, Not 120L Total Volume

The supplied capacity figures describe different things: 120L is the total main-vessel capacity, 100L is the specified working capacity, and 20L is the listed minimum batch size. Production planning should preserve those distinctions rather than treat the total vessel volume as a routine production batch.

A 100L working capacity is not a promise of 100L of saleable product after every batch. Transfer losses, retained material, sampling, and the formulation process affect the quantity reaching the filling stage. Likewise, liters should not be converted directly into kilograms without the product density.

Use the intended batch size as a starting point, then review the complete production sequence. Preparation, heating, charging, emulsification, cooling, discharge, and cleaning all occupy time. The vessel capacity alone cannot establish batches per shift or daily output.

If demand would require frequent operation beyond the specified working capacity, evaluate a larger model rather than planning to use the nominal headspace as additional production volume. The 1000L PLC external circulation emulsifying mixer is one larger-system reference. It is not a direct substitute based on capacity alone: compare its processing arrangement, utilities, access, and verified batch requirements separately.

Evaluate the Lowest Batch Size Separately

The listed 20L minimum batch size offers a useful starting point for discussing smaller production runs. It does not demonstrate that every cream or lotion will circulate and homogenize effectively at that volume.

At the lower end of the range, confirm that the processing elements engage the product as intended. A trial should examine bulk movement, feed incorporation, behavior around the bottom homogenizer, and the ability to control the product throughout the process. A small batch that can physically fit in the vessel is not automatically an effective processing batch.

This matters when a manufacturer plans to use the same machine for product development, market trials, and routine production. Agree the smallest commercially important batch before purchase and include it in the sample evaluation.

If most planned batches fall below the stated minimum, evaluate a dedicated development machine such as the 5L lab circulation vacuum emulsifier. Its standalone arrangement and trial workflow should be assessed separately rather than treated as a smaller copy of this three-vessel production system.

Use the Oil and Water Pots According to the Formula

The integrated auxiliary vessels are specified as a 50L oil pot and an 80L water pot. Their capacities support separate phase preparation, but should not be added together to calculate the main tank’s batch size.

The correct allocation depends on the formula’s phase proportions, ingredient behavior, and charging sequence. A recipe with a large aqueous phase has different preparation needs from one with a substantial oil phase or ingredients added later during cooling.

Before ordering, map the formulation stages to the three vessels. Identify which ingredients are prepared separately, which enter the main tank directly, and when temperature-sensitive or fragrance ingredients are added. The fragrance and active-ingredient addition guide provides supporting context for that review.

Confirm the actual heating, agitation, and transfer provisions of the auxiliary pots rather than assuming they match the main vessel. This review can reveal whether the supplied preparation arrangement fits the intended product family or whether a particular formulation needs a modified workflow.

Select Hydraulic Lifting for Access Requirements

The hydraulic lifting head provides access to the main vessel between processing operations. It is particularly relevant when inspection, cleaning access, or maintenance access forms an important part of the production plan.

The benefit comes with installation requirements. The supplied fully raised height is 2800 mm, and the final layout must allow additional clearance specified for safe operation and service. Review ceiling obstructions, overhead services, lighting, and access routes before approving the location.

A fixed-head system may deserve consideration when the operating arrangement does not require routine lifting. The fixed-head vacuum emulsifying mixer product page provides an alternative architecture to review, although its capacity and installation requirements differ. Do not assume that a fixed-head model will fit a restricted space without checking its own drawings.

Hydraulic lifting should be selected because its access function serves the process, rather than because it is assumed to improve emulsification. During an equipment review, ask to see the head-opening and access sequence. Confirm which components move with the head, which remain in the vessel, and how the manufacturer requires the vessel to be made safe before lifting.

Match Agitation and Homogenization to Product Behavior

The helical ribbon agitator, PTFE wall scrapers, and bottom-entry rotor-stator homogenizer perform different roles. The agitator handles bulk movement, the scrapers act along the wall, and the homogenizer supplies localized high shear.

Independent speed control allows the operating settings to be selected for the formulation. It does not establish that the highest available speed gives the best product. A formulation may need different settings during ingredient incorporation, emulsification, cooling, and finishing.

For a comparison within the same working-capacity class, review the 100L button-control vacuum emulsifying mixer. That configuration uses gate agitation with fixed paddles and an operator-led semi-automatic workflow. The choice involves the agitation arrangement and operating method, not simply the appearance of the control panel.

The supplied maximum viscosity for this model is 50,000 cP, but viscosity changes with temperature and can depend on how the material is measured. Products with similar reported viscosity may differ in yield behavior, flow, or shear sensitivity. Provide the measurement conditions and processing temperature when discussing a high-viscosity application.

Define the required result before a trial: appropriate uniformity, acceptable air content, desired appearance, or another agreed product criterion. Do not replace those criteria with an unsupported claim that one rotor speed guarantees a particular droplet size or emulsion stability.

Confirm the Complete Heating and Cooling Duty

The main vessel uses jacket heating, with electric heating specified and external steam heating listed as an option. The appropriate choice depends on the site’s utilities, required temperature profile, and production schedule. The steam versus electric heating guide provides supporting technical context.

The supplied temperature-control accuracy is ±1°C. Before treating this as a finished-product temperature guarantee, confirm the measurement location, operating conditions, and acceptance method. A control-system figure does not by itself describe temperature uniformity throughout every formulation.

Cooling deserves the same attention as heating. Tap water or cooling-tower circulation may suit some duties, while chilled-water or glycol circulation may be required for others. Select the supply against the actual thermal requirement rather than assuming that an optional chiller is always necessary.

Ask for the required utility conditions and the basis for any proposed cooling time. Review the relevant utility systems alongside the mixer configuration. The listed total electrical power does not establish the cooling duty or the duration of a complete batch.

Choose Discharge Around the Receiving Process

Electric tilting, bottom-valve discharge, and external pump transfer are listed discharge arrangements. The practical choice depends on product flow, receiving-container position, transfer distance, and the equipment downstream.

A flowable lotion and a structured cream may behave differently during emptying. Review whether the product can move through the selected outlet at its discharge temperature and whether the transfer method suits its shear sensitivity and handling requirements.

Where external transfer is required, the portable rotary lobe pump product page provides a specific equipment option for evaluation. Its suitability, connections, and operating conditions must be confirmed for the actual product rather than assumed from the pump type.

The flush bottom valve is a specified feature, but it should not be presented as proof of zero retained product or completely residue-free discharge. Assess the actual emptying result with the intended formulation. The product recovery guide provides a related assessment resource.

Pressure-assisted discharge requires separate engineering confirmation. The jacket’s stated design pressure is not a pressure rating for the product chamber. An available compressed-air connection must not be treated as authorization to pressurize the main vessel.

Define Cleaning Scope Beyond the Spray Ball

The machine includes a CIP spray ball and a specified polished SUS316L product-contact interior. These provisions support cleaning planning, but do not establish a validated automatic cleaning cycle. The CIP spray ball versus manual cleaning guide explains a related scope distinction.

Agree how cleaning solution is supplied, which surfaces are reached, how return flow is managed, and which components need separate attention. The bottom homogenizer, mechanical seal, discharge valve, ports, and head-mounted accessories should be considered in the cleaning procedure.

The hydraulic lifting arrangement can provide inspection access, but cleaning effectiveness still depends on the product residue, procedure, and acceptance criteria. The hygienic equipment design guide provides supporting context for reviewing product-contact details. A visually clean vessel is not sufficient evidence for every product-changeover requirement.

Where a separate CIP unit is proposed, define its scope explicitly. Do not assume that spray-ball provision includes chemical dosing, heating, automatic sequencing, or verified cleaning performance.

Specify Controls and Mechanical Seals in the Order

The supplied information confirms PLC and HMI control, but lists different HMI brand possibilities. The purchase specification should identify the final PLC, HMI, drive, motor, and electrical component selections.

Also define the control functions that matter to production. Recipe storage, process recording, automatic ingredient dosing, remote access, and line communication are separate requirements; they should not be inferred from a touch screen or a general automation label.

Mechanical-seal alternatives include single- and double-seal arrangements with listed brand options. Select the actual arrangement against the product, temperature, vacuum conditions, and the manufacturer’s recommendations. Confirm any cooling or support requirements before utility planning is finalized.

The published mechanical-seal cooling-water case study provides a related reference without establishing identical service requirements for every seal configuration.

Clear component and function schedules make the delivered configuration reviewable and provide a more useful basis for maintenance planning than a list of optional brand names.

When This 100L Model May Be the Wrong Choice

A larger vessel may be more appropriate when the required batch exceeds the 100L working capacity. A smaller system may be preferable when the main requirement is repeated development work below the listed minimum batch size.

A simpler mixing tank may also deserve evaluation when the formulation does not require vacuum or high-shear emulsification. The open-top jacketed mixing tank product page provides a different vessel-based configuration to review. It is an alternative equipment approach, not a capacity-equivalent replacement.

For dispersion-led work, review a dedicated option such as the hydraulic lifting high speed disperser. A dispersing element and a rotor-stator homogenizer should not be treated as interchangeable, and suitability must be assessed for the intended material.

Products outside the stated viscosity range, or processes with separately defined containment or hazardous-area requirements, need a different or modified equipment assessment. Restricted lifting clearance can also make the hydraulic arrangement unsuitable even when the vessel capacity is correct.

Prepare a Model-Specific Purchase Checklist

• Confirm routine, minimum, and largest intended batch sizes
• Provide formulations or representative product characteristics for review
• Define viscosity together with its temperature and measurement conditions
• Map phase preparation to the oil, water, and main vessels
• Agree heating and cooling requirements and available utilities
• Confirm raised-head clearance and the installed operating envelope
• Select the mechanical seal and its support requirements
• Define discharge, receiving, and downstream transfer arrangements
• Specify the actual controls, component brands, and required functions
• Agree sample trials, acceptance criteria, documentation, and training scope

StriversMachinery manufactures core equipment in-house and sources complementary equipment from long-term partner manufacturers. The manufacturing and integrated-supply explanation provides further context.

StriversMachinery takes responsibility for complete production line integration and delivery. For this 100L system, the agreed technical specification should connect the vessel configuration with the customer’s preparation, transfer, storage, and filling equipment requirements.