• Feeder system for solvents (central or decentralized preparation, buffer container, avoidance of incompatible media) 
• Dosing system for reaction partners (portioning or continuous feeding) 
• Agitated, temperature-controlled reactor with distillation system (jacket/half-coil pipes, additional internal and external heat transfer surfaces, central media supply or assigned heating/cooling units, cool/cold/cryogenic) 
• Vacuum condensation system (dry-running vacuum pumps, liquid-ring pumps; condensers cool/cold/cryogenic) 
• Co-reactor for phase separations 
• Separation and drying of solids (either separate process stages or a filter-dryer combination) 

In the case of multi-purpose plants, either reference syntheses and their minimum requirements are defined, or the limit values for using the plant are derived from the configuration.

• The plant is designed for largely automated operation. This means that the technical field conditions have been implemented for complete recipe control. The subsystems are operated and monitored by a central process control system. The elements relevant to GMP are qualified. 
• Only some individual phases (such as dosing) run automatically. Batch logs are generated from the registered process variables and events that document the batch production. 

The plant uses hazardous substances subject to the Hazardous Substances Order, which have the following properties: extremely flammable, highly flammable, very toxic, toxic, harmful, irritant, corrosive, sensitising, an occupational exposure limit value. Notices are available that describe the CMR properties of the substances used: EU category 2 or 3 (GHS category 1B or 2). A hazardous explosive atmosphere can develop in the plant area as per (TRBS (German Technical Rules for Operational Safety) 2152 Part 1. Liquids subject to the German Water Ecology Act are used in the plant (plant for producing, treating and using substances). 

• High pressure polymerization to produce polyethylene waxes
• High pressure polymerization to produce polyethylene vinyl acetate copolymers
• Polymerization in an agitator vessel to produce norbornene ethylene copolymers
• Synthesis in an agitator vessel to produce formaldehyde reducing agents
• Synthesis in an agitator vessel to produce bleach activators
• Synthesis in an agitator vessel to produce trimethylolpropane
• Continuous gas/liquid reaction to produce hexamethylenetetramine
• Rotary, thin-film evaporator and spray tower to produce granulated paraformaldehyde
• Catalytic gas phase reaction to produce dimethyl ether
• Continuous gas/liquid reaction to produce dimethyl formamide
• Synthesis in an agitator vessel to produce glycidyl ether
• Synthesis in an agitator vessel to produce epoxy resin

(Hydration reactor for synthesizing hexenol at 100 bar(g) in a salt bath reactor at +400 °C)

On the other hand, diverse reactions are controlled in a low temperature range

(Highly reactive substances, selective isomerisation, etc.)

• Alcohols, alcohol mixtures (e.g. methanol, ethanol, ethylene glycol, isobutylol)
• Aromatics, phenols (e.g. benzene, ethyl benzene, cumene, phenol, xylenes)
• Amines, amides (e.g. dimethylamine, trimethylamine, monomethylamine, formamide, methyl formamide, dimethyl formamide)
• Monomers for polymer production (e.g. norbornene, dicyclopentadiene)
• Chlorinated hydrocarbons (e.g. dichloromethane)
• Ketones (e.g. cyclohexanone)
• Carboxylic acid derivates (e.g. fatty acid methyl esters, fatty alcohols)
• Extractive distillation (e.g. butene-butadiene separation)
• Dehydration of products
• Separation of solvents from substances with relatively high boiling points (e.g. epoxy resin)
• Thermally gentle rectificative processes
• Reactive distillation (chlorosilanes)