PROSALT EVAPORATION TECHNOLOGIES

Energy.A second life.

Turnkey evaporation.
Engineering, in-house manufacturing and site installation. One responsible team: PROSALT.

Concept studio image of a stainless steel evaporation system
Start exploringCONCEPT SYSTEM IMAGE

A NEW PERSPECTIVE ON THE SAME ENERGY.

Water evaporates. Value remains. A cycle reimagined through engineering.

Systems that recover heat energy, support water reuse and focus on your product. Designed to find the right balance for every process.

01Preserve energy.

Recover the heat in vapor.

02Recover water.

Reuse condensate according to its quality.

03Focus on the product.

Design for the target concentration.

THREE TECHNOLOGIES. ONE APPROACH.

Built around your process.

Concept MVR evaporation unit
01 / MECHANICAL VAPOR RECOMPRESSION

One vapor stream.
New potential.

Mechanical compression turns process vapor back into a heat source. An electrically driven way to keep energy within the cycle.

VaporCompressorHeating
MVRCONCEPT SYSTEM IMAGE
Concept industrial evaporation plant
02 / THERMAL VAPOR RECOMPRESSION

Your existing steam.
More value.

Motive steam entrains part of the process vapor in an ejector. The resulting mixture returns to the heating side.

VaporEjectorHeating
TVRCONCEPT PLANT IMAGE
Concept flash evaporation unit
03 / FLASH EVAPORATION

Pressure changes.
Value is released.

Hot liquid partially evaporates at lower pressure. Heat and pressure are managed in a single- or multistage system tailored to the process.

Hot feedPressure dropPhase separation
FLASHCONCEPT SYSTEM IMAGE

Scroll to explore. Or choose a technology.

MVR / ENERGY CYCLE

The journey of a drop.

Single effect · Forced circulation · MVR

Liquid pathVapour pathHeat transferCondensate

Auxiliaries: start-up heat and non-condensable gas removal.

01 / 05

Feed and circulation

Feed joins the liquid returning from the separator. The circulation pump sends the mixture through the heat exchanger; product is withdrawn through a separate branch.

Scroll or choose a step.

Defined process arrangement, not a final plant design or P&ID. Auxiliary circuits and controls are not detailed. Line crossings without dots are not connections.

A BIG DIFFERENCE IN SMALL DETAILS.

Closer reveals
more.

From materials to maintenance access.
Every detail, considered together.

Concept close-up of stainless surfaces and pipe connections
CONCEPT MATERIAL IMAGE
PROSALT DELIVERY MODEL

Engineering, manufacturing and turnkey installation under one roof.

One team considering the entire plant and taking responsibility for your project.

Engineering

We define the scope together.

Starting with feed analysis, capacity and product targets, we prepare process, layout and foundation designs. Acceptance conditions and delivery boundaries are defined at the start.

Manufacturing and integration

We manufacture in-house and integrate the system.

We manufacture process equipment and structural steelwork in-house. We take responsibility for electrical and automation systems and the integration of selected motors, compressors and instruments.

Installation and commissioning

The same responsibility on site.

We coordinate mechanical and electrical installation, system checks and commissioning. Maintenance access and equipment removal space are considered from the design stage.

Operational handover

Operation after handover is part of the plan.

Operator training, operating and maintenance documents, critical spares and support scope are defined within the project. Acceptance is assessed against agreed feed and operating conditions.

You prepare the foundations. We provide the design.

The customer carries out concrete and foundation works to the designs and technical requirements provided by PROSALT. PROSALT takes responsibility for equipment, structural steelwork, electrical systems, automation and site installation.

Clear scope. A direct point of contact.

Project contacts, progress updates and site coordination are planned at the outset. Utility connection points, site preparation and local approval responsibilities are clarified in the proposal.

Discuss your delivery scope

SIDE BY SIDE

Which fits your process?

The right choice starts with your process conditions.

Compare MVR, TVR and Flash
Key differences between MVR, TVR and flash technologies
CriterionMVRTVRFLASH
Operating principleMechanical vapor compressionRecompression with a steam ejectorEvaporation by pressure reduction
Main energy inputSteam and electricityMotive steamFeed heat / external heating
Selection focusElectricity price, temperature differenceSteam pressure and costAvailable heat, pressure stages
Key equipmentCompressor or fanThermocompressorFlash vessel and vacuum system

Final selection depends on product analysis, capacity, energy prices and operating conditions. Flash stages may also be combined with other heat recovery methods.

PROCESS ENGINEERING

From solution to product. Consider every stage.

Product targets, available utilities and solution behaviour are assessed together.

Energy integration

MVR uses mechanical compression; TVR uses motive steam. In multiple-effect evaporation (MEE), vapour from one effect heats the next. Selection considers the available temperature difference, energy prices and annual operating hours.

Evaporator selection

Evaluated for non-precipitating applications requiring short residence times. Forced circulation is evaluated for crystal-bearing or scaling-prone fluids. In circulating crystallizers, boiling inside the heater can be suppressed so evaporation occurs in the separator.

Crystal and product quality

Target particle-size distribution is considered alongside supersaturation, residence time and crystal breakage. DTB or growth-type crystallizers are evaluated against this target. Solid-liquid separation and residual moisture determine the load on subsequent drying.

Recrystallization

Recrystallization aims to separate impurities by dissolving solid salt, purifying the solution and forming crystals again. Evaporation or cooling is selected according to solubility behaviour. Mother-liquor recycle and purge are balanced to control impurity accumulation.

Data for process design

Feed ion analysis and variability; flow, temperature, density and viscosity; target purity, particle size and moisture; steam, electricity and cooling conditions; annual operating hours and site constraints. Mass and energy balances, with sample tests where needed, underpin equipment selection.

This content explains general process principles. PROSALT project scope and performance values are determined from feed data and engineering assessment.

Start with your process data

EXPLORE YOUR PROCESS

Your data.
A clearer starting point.

Choose your goal first, then continue with the data you know. We can clarify missing information during the technical discussion.

Start with your goal.

01 / PROCESS INPUTS

Initial values are an example. Replace them with your process data.

Enter your own process values before adding a calculation to your enquiry.

02 / PRELIMINARY MASS BALANCE

See the outlet streams.

Example calculation

Feedt/h
Concentrate outlett/h
Water to evaporatet/h
Conserved nonvolatile solutet/h

Method and limitations

Assumes steady state, pure water vapor, complete solute retention, no losses and no crystallization. Percentages are by mass, not volume.

C = F × x₁ / x₂   ·   V = F − C

F: feed, C: concentrate, V: evaporated water. x₁ and x₂ are initial and target mass percentages of the same component.

This is not a heat balance or equipment capacity guarantee. Target concentration feasibility must be checked against solubility, viscosity and temperature.

03 / TECHNOLOGY SCREENING

What does your energy infrastructure suggest?

This is preliminary screening. Final selection requires product analysis, mass and energy balances, operating hours and energy costs.

Use these inputs to start your technical discussion.

YOUR NEXT CYCLE.

It starts with an idea.
Takes shape together.

Tell us about your process. Our engineering team will get in touch.

PROJECT START / 01

What
can we
make possible?

Application, technology and capacity.
Three essentials for the first step.

Your enquiry is emailed directly to [email protected]. No document download is needed.

Select this option if capacity is unknown. We can clarify it together during the technical assessment.

We use your details to respond. Your message is sent via Resend and may be translated into Turkish by DeepL; the original is retained in the email. Contact fields are not sent for translation.

[email protected]

TECHNICAL DISCUSSION

Let's assess
your process together.

Share your feed analysis, target capacity and available energy sources. Our team will help define the next step.

YOUR QUESTIONS

A little
closer.

Is MVR the best choice for every application?

No. Electricity and steam prices, operating hours, boiling point elevation and product properties must be assessed together. Technology selection is project-specific.

How are materials selected?

Chloride content, temperature, pH, corrosion and cleaning conditions determine the choice. Stainless steel grades or special alloys are selected using product analysis and process conditions.

Does evaporation alone achieve zero liquid discharge?

Not always. Zero liquid discharge requires an integrated assessment of pretreatment, evaporation, crystallization and solid–liquid separation.

What information is needed for an initial technical assessment?

Feed flow and composition, initial and target concentration, operating hours, steam and electricity conditions and site layout are the key inputs.