
In a chemical plant the reactor is where the product is actually made; everything else feeds it, cools it or takes product away. A typical reactor package includes the main vessel, a vertical or horizontal condenser and a decanter for phase separation, all sized around one shared set of process conditions rather than picked independently.
The general operating requirements are similar across most duties: operation under pressure or vacuum, controlled mixing, and heating and cooling through a jacket or coil. What differs between applications is how far each requirement is pushed, and that’s what the design work is actually about.
The four parameters that drive the design
Four parameters set the mechanical design: working pressure, working vacuum, working and cooling temperature, and the required heating and cooling time.
- Working pressure and vacuum set the wall thickness, head type (flat, dished or hemispherical) and nozzle reinforcement, and determine whether the vessel needs to be designed and stamped to a pressure-vessel code such as ASME VIII or the European PED, or can be built as an atmospheric vessel.
- Working and cooling temperature set material selection (not every stainless grade performs the same at both temperature extremes a batch process can see) and drive the jacket design: a full jacket, a half-pipe coil, or a dimple jacket, each with different heat-transfer coefficients and pressure ratings.
- Heating and cooling time is the parameter most often underestimated. A customer will specify a batch cycle time without realising that the time budget for heat-up and cool-down is what actually sets the heat-transfer area, which in turn sets the jacket or half-pipe coil design and the utility (steam, thermal oil, chilled water) demand on the rest of the plant. Undersize this and the batch cycle simply runs longer than planned for the life of the equipment.
Agitation and internals
Mixing duty is set independently of the four parameters above but interacts with all of them: viscosity, whether the reaction is single- or multi-phase, and whether solids need to stay in suspension all affect impeller type and drive sizing. Baffles, dip pipes, spray balls for CIP and sample/dosing nozzles are placed according to the process flow diagram, not as standard fittings: a reactor’s nozzle schedule is effectively a map of every other piece of equipment connected to it.
Materials, welding and finish
Reactor shells are most commonly built in 304/304L or 316/316L stainless steel, with grade selection driven by chloride exposure and cleaning chemistry rather than by pressure alone. Welding is done under qualified procedures: TIG for shell and nozzle welds, orbital welding where a consistent, contamination-free internal bead matters, such as in pharmaceutical and food service. After welding, the vessel is pickled and passivated to restore the chromium-oxide layer that welding heat disrupts, and the internal finish (2B mill, brushed, or mechanically/electro-polished) is specified to match the cleaning and hygienic requirements of the product.
Makfen designs and fabricates reactors in stainless and carbon steel against these parameters, with material certificates and pressure-test records issued for each vessel.
- Reactor design
- Process engineering
- Stainless steel reactor
- Heat transfer
- Pressure vessel
