
3M, ABB, AES, Agip, Akzo, Albemarle. Alzchem, AMI, Amoco, Amylum, Aptec, Aramco, Arco, AspenTech, BASF, Bayer, Bayernoil, Bharat, Biochemie, Borealis, BP, BRC, Cargill, Cemex, Chemserv, Clariant, Cognis, Corus, CSLBehring, cts-GmbH, Currenta, Degussa / Evonik, Donau Chemie, Dow, DSM, Dyneon, EC-Erdölchemie, EDL, Elmont, E.ON, Esso/Exxon, Eurotherm, Fina, Foxboro/Invensis, Gunvor, Hoechst, Honeywell, Huels, Ineos, Infineum, Lang & Peitler, Lanxess, Laporte, Lenzing AG, Linde, LyondellBasell, KNPC, MIRO, MSD, Neste, Novartis, Nynas, OMV, PCK Schwedt, Petronas, Phenolchemie, Provadis, Reliance, Repsol, Rhöm, Roche, Ruhr Öl, RWE, Sabic, Saras, Sasol, Shell, Siemens, Sipchem, SPE, Solvay, Spiratec, Sunkyong, Sunvic, Taminco, Tessenderlo Chemie, TET, ThyssenKrupp, Total, Treibacher AG, Vinnolit, Vinythai, UCB, Wacker, Xervon, Zellstoff Stendal, many engineering companies, universities and technical colleges.
Some examples of ACT's international consulting and engineering work are:
Power plant | Czech Republic | Incentive study for the change from the existing analog instrumentation to a Distributed Control System |
Chemical plant | The Netherlands | Incentive study for the upgrade of the existing DCS, feasibility and economics of combining several control houses into one control center |
Styrol plant | Belgium | Advanced control study. Definition of improvements of current controls and of additional advanced controls, application design basis document (DBM) |
Glycol plant | Belgium | Advanced control study. Performance improvement of current controls, definition of additional advanced controls, incentive estimation, applications DBM |
Amine plant | Belgium | Advanced control study. Definition of attractive additional controls, incentive estimation and application design basis document, implementation plan |
Chemical plant | Belgium | Adaptive model based control of a fed-batch reactor for Polyether production. (Complete application development and tuning was achieved in one day) |
Chemical plant | Germany | Development and implementation of strategies for stabilization of a highly integrated unit and for throughput maximization |
Oil refinery | Germany | Middle distillate yield maximization using an EVOP approach |
Chemical plant | Germany | Reduction of batch cycle time and improvement of the temperature performance on various fed-batch reactors |
Oil refinery | Malaysia | Bid specification for a production planning and product apportionment system |
Oil refinery | India | Development and implementation of advanced product quality strategies for a delayed coker unit |