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Chemical Process Agitators

Agitators for reaction, gas-liquid, crystallization and suspension duties, sized from your process data and designed for your pressure and corrosion conditions.

150 bar
HP Series Operating Pressure
40 m³
RC-M Reactor Volume, Up To
100,000 cP
Viscosity, Up To
Industrial reactor and agitator for chemical processing

What Does an Agitator Do in a Chemical Process?

In a chemical process, the agitator brings reactants into contact, carries heat to the jacket and coils, disperses gas and a second liquid phase, and keeps solids in suspension. If the duty is defined incorrectly, by-products increase, reaction time grows, crystal size drifts and heat control weakens. Mechanimix first identifies the step that limits the process, then sizes the impeller, power, materials and sealing for that duty.

Separate duty definitions for blending, mass transfer and heat transfer
GM, GDM and GDS impellers for gas-liquid reactions
Material options from AISI 316L to Hastelloy and Titanium
We can design for ATEX and Ex-proof requirements
PROCESSES

Mixing Duties in Chemical Processing

The same reactor volume needs a different agitator in a different process. Here is the duty, the main risk and our approach for each one.

Batch and Continuous Reactions

Agitator duty
Bring reactants into contact quickly, even out temperature and concentration across the reactor, and carry reaction heat to the jacket or coils.
Critical risk
If blend time is longer than reaction time, by-products increase. In semi-batch feeding, a stopped agitator lets reagent accumulate, and the heat can be released all at once on restart.
Our solution
HWM, HWM-B or HVM by viscosity, with the feed point placed in the high-flow zone. RC-M reactors can monitor torque and temperature, and stopping the feed when the agitator stops is written into the control logic. For polymer reactions, see Plastics.

Neutralization and pH Adjustment

Agitator duty
Disperse acid or base into the main stream quickly, even out pH across the full volume and carry away the heat of neutralization.
Critical risk
Local pH and temperature spikes at the feed point precipitate salts or damage the product. With a steep titration curve, the pH reading oscillates and chemical is wasted.
Our solution
HM or HWM for high pumping. The dosing point goes in a strong flow zone and the pH probe is placed with blend time in mind. In continuous lines, a static mixer can handle pre-mixing.

Hydrogenation

Agitator duty
Disperse hydrogen into the liquid, keep solid catalyst suspended and remove reaction heat. Reaction rate is often limited by gas-liquid mass transfer (kLa), not by the chemistry.
Critical risk
Low kLa extends reaction time, and settled catalyst harms selectivity. Under pressurized hydrogen, the shaft seal is the most critical safety item.
Our solution
Self-aspirating GM, which draws headspace gas back into the liquid, or GDM with a sparger. HP Series from vacuum to 150 bar, and HPR reactors at small scale. See Hydrogenation.

Chlorination, Oxidation and Gas Absorption

Agitator duty
Disperse gases such as chlorine, oxygen, air or CO₂ as fine bubbles and increase bubble residence time in the liquid.
Critical risk
When gas flow exceeds the impeller's limit, flooding starts and gas reaches the surface without mixing in. In chlorination, moisture, chlorine and HCl make material selection the first design decision.
Our solution
GDM for high gas rates, and GDS where gas pockets are a risk or solids must also stay suspended. Materials follow the environment: Hastelloy and Titanium are assessed, but Titanium is considered for wet chlorine only and is not used in dry chlorine.

Crystallization and Precipitation

Agitator duty
Keep crystals suspended, even out temperature and supersaturation across the tank, and limit local supersaturation at cooling surfaces.
Critical risk
High tip speed breaks crystals, and secondary nucleation creates fines that make filtration and drying harder. Scaling on cold walls reduces heat transfer.
Our solution
Low-shear HWM-B and TVM. The starting tip speed range is 1–3 m/s, with the final value set by the crystal size target. See Crystallization and Crystallization Systems.

Dissolving and Dilution

Agitator duty
Wet out and dissolve powders and granules without lumps, and dilute concentrated acids and bases in a controlled way.
Critical risk
Powder floats or forms lumps on the bottom, which extends dissolving time. Sulfuric acid and caustic dilution release heat that can cause local boiling, and intermediate concentrations in the dilution zone can be more aggressive to materials.
Our solution
HM or HWM placed to draw floating solids down or lift sinking solids from the floor. In dilution, the feed goes in a strong flow zone, and heat balance and materials are checked across the full concentration range.

Solids Suspension and Slurries

Agitator duty
Keep solids such as catalyst, pigment, salts, phosphate rock and gypsum suspended, and draw product at a uniform concentration.
Critical risk
Corrosion and abrasion act together in phosphoric acid and fertilizer slurries. Starting in settled solids after a power failure is far heavier than normal running.
Our solution
HWM, HWM-B or TVM, with TVM for tall tanks (H/T > 1.5). Just-suspended speed starts from the Zwietering correlation. NP-H agitators offer Duplex, Super Duplex and rubber, polyethylene or ceramic coating options.

Liquid-Liquid Extraction and Dispersion

Agitator duty
Disperse two immiscible phases to increase contact area, providing mass transfer for extraction, washing and phase-transfer reactions.
Critical risk
Too much energy creates very fine droplets, so phase separation slows and a stable emulsion can form. Too little energy reduces contact area and yield.
Our solution
Droplet size is set by power density and tip speed, starting from Weber number correlations. HM with adjustable blade angle, plus speed adjustment with a VFD where needed. The continuous phase and start-up sequence are defined in the design.

Storage and Blending Tanks

Agitator duty
Keep raw material, intermediate and finished product tanks homogeneous, blend additives and prevent settling.
Critical risk
Density differences cause stratification. A sample point can look fine while part of the product is off-spec.
Our solution
NP Series for small and medium tanks, and VMG, HMG and HMB side-entry agitators for large volumes. Unit count and layout follow the blend time target.
SELECTION GUIDE

7 Critical Questions When Selecting a Chemical Agitator

Clarifying these points before you request a quote leads to the right design and the right price.

CriterionWhy it mattersHow we handle it
Main duty and number of phasesLiquid-liquid, solid-liquid and gas-liquid duties need different impellers and power. With three phases present, the limiting duty decides.We write down the limiting step first: blending, mass transfer or heat transfer. The impeller follows from that, with different stages where needed.
Reaction heatOn scale-up, volume grows with the cube of diameter while jacket area grows with the square. Heat that is no issue in the lab can limit production.A heat balance is built for the worst moment. If the jacket is not enough, a half-pipe jacket, coils or a dosing profile are assessed.
Viscosity and rheologyTurbulence fades as Reynolds number falls: roughly laminar at Re < 10 and turbulent at Re > 10,000. In the laminar range, an axial impeller only mixes its immediate surroundings.Viscosity is tracked across temperature and conversion. HWM is assessed up to about 1,000 cP, and HVM for more viscous media up to 100,000 cP.
Pressure, vacuum and sealingPressure brings a risk of product leakage and vacuum a risk of air ingress. Product toxicity and flammability set the sealing level.NP Series for atmospheric tanks, HP Series from vacuum to 150 bar. Single, double or dry-running seals or a magnetic coupling are selected by product.
CorrosionConcentration, temperature, chlorides and oxidizing conditions determine material life. The same acid behaves differently at different concentrations.AISI 316L, Duplex, Super Duplex, Hastelloy or Titanium are selected from the process chemistry, taking cleaning and shutdown conditions into account.
Tank geometry and internalsBaffles, coils, dip pipes and operating level change the flow. At low level, an impeller near the surface starts drawing air and causing vibration.Lowest and highest levels are checked together. Impeller position, stage count and baffle layout are calculated, with CFD on higher-risk duties.
Explosive atmospheresWith solvent vapor, hydrogen or combustible dust, the motor, sensors, sealing and accessories must be assessed together.We can design for ATEX and Ex-proof requirements. Share your hazardous area data at the quotation stage.
ENGINEERING

Design Details That Matter in the Field

Sealing

Single and double mechanical seals, dry-running seals and magnetic coupling options, selected by pressure, temperature, product hazard and maintenance access.

Wetted Materials

AISI 316L, Duplex, Super Duplex, Hastelloy and Titanium, with rubber, polyethylene or ceramic coatings where needed. Selection also considers intermediate concentrations and cleaning conditions, not only the product.

Shaft and Bearings

The shaft is calculated for critical speed and impeller loads. A rigid bearing housing limits deflection and vibration at the seal.

Explosive Atmospheres

We can design for ATEX and Ex-proof requirements in areas with solvent vapor, hydrogen or combustible dust.

HOW WE WORK

From Process Data to a Running Agitator

  1. Process dataWe define the duty first: fluid or slurry properties, tank geometry, operating conditions and the result you need.
  2. Hydraulic sizingImpeller type, diameter, speed and power are calculated from that duty, not picked from a catalogue.
  3. CFD validationWhere the risk justifies it, flow, dead zones and blend or suspension behaviour are checked before manufacturing.
  4. Mechanical design and deliveryShaft, bearings, seal, materials and drive are designed for the loads; supply, installation support and commissioning follow.

Recommended Equipment for This Sector

The right equipment follows from the process duty. These are the starting points.

Top-Entry Agitators

NP Series for atmospheric tanks and HP Series for pressurized reactors.

View details →

Stainless Reactors

RC-M and RC-L for production, RP for pilot work and HPR for high pressure.

View details →

Vacuum Dryers

VD-M, VD-R and VD-P series for heat-sensitive products after crystallization and precipitation.

View details →
FAQ

Frequently Asked Questions

Which impeller is used in a chemical reactor?+
The impeller is selected for the duty that limits the reactor. HWM and HWM-B lead for liquid blending and heat transfer, HWM, HM and TVM for solids suspension, GDM, GM and GDS for gas-liquid reactions, and HVM for high viscosity. Where several duties apply, different stages can be fitted on the same shaft.
Which agitator is used in a hydrogenation reactor?+
Hydrogenation needs an agitator with a gas dispersion impeller and sealing suited to the pressure. Self-aspirating GM draws headspace hydrogen back into the liquid and needs no external sparger, while GDM with a sparger is selected for high gas rates. HP Series covers vacuum to 150 bar, and HPR reactors are assessed at small scale.
What is flooding in gas dispersion and how is it prevented?+
Flooding is when gas flow exceeds what the impeller can disperse and gas reaches the surface without mixing in. Prevention means selecting gas rate, speed and impeller type together. GDM is designed for high gas rates, and GDS combines radial and axial flow to prevent gas pockets.
How is mixing speed set in crystallization?+
Mixing speed is set close to the lowest value that keeps crystals suspended. A tip speed of 1–3 m/s is the starting point, and the final value depends on crystal size target, solids content and density difference. High speed causes breakage and secondary nucleation, while low speed causes settling and local supersaturation.
Which impeller is used for high-viscosity chemicals?+
High-viscosity duties use the HVM impeller. With its narrow blade geometry, HVM works in laminar flow from 500 to 100,000 cP and can rotate in both directions. Where wall residue is a problem, the PTFE-scraper anchor agitator in RC-L reactors is assessed.
Should a reactor use a mechanical seal or a magnetic coupling?+
The choice depends on pressure, torque and product hazard. Double mechanical seals with barrier fluid are common in high-torque and large reactors. A magnetic coupling removes the dynamic shaft penetration, but transmissible torque is limited and internal bearings need checking with solids-bearing products.
What matters for an agitator in an acid dilution tank?+
In acid dilution, heat and corrosion must be managed together. With products such as sulfuric acid, concentrated acid is fed into water in a controlled way, and the feed point should be in a strong flow zone. Materials are selected for the intermediate concentration and temperature in the dilution zone, not only the final concentration.
Which material should a chemical agitator use?+
Material is selected by concentration, temperature, chlorides and cleaning conditions, not by a chemical name alone. AISI 316L is the starting point for most media, Duplex and Super Duplex are assessed as chlorides rise, and Hastelloy or Titanium for more aggressive media. Titanium is considered for wet chlorine and is not used in dry chlorine.
How is a lab recipe scaled up to a production reactor?+
A lab recipe is scaled by preserving the step that limits the process. Power density, tip speed and blend time cannot all stay constant, so the process decides which one to keep. Data from an RP pilot reactor is carried to production scale, and CFD checks flow and dead zones before manufacturing on higher-risk duties.
What data is needed for a chemical agitator quote?+
Process duty, phase information, density and viscosity range, temperature and pressure, tank dimensions, internals and hazardous area data are a sufficient start. Gas-liquid duties also need gas flow rate, and solids duties need particle size and solids content. We can build assumptions together for any data you do not have.

Tell Us About Your Reactor and Process

Start with your reaction, phase and vessel data. We will define the duty and size the right agitator with you.

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