1. Process Integration Ltd

2. Activity type PIL RTD/Innovation activities WP11.5 WP21.5 WP30 WP42 Total Research5 Demonstration activities WP52 Total Demo2 Consortium Management activities Total Management6 Other activities WP60 Total other0 Total13

3. PIL in WP1 Task 1.1. Experimental fouling investigation Collaboration with UNIBATH, CALGAVIN, UNIMAN, UPB on kinetics of fouling and incorporation of the data into the models being developed

4. PIL in WP2 Collaboration with UNIBATH, CALGAVIN, UNIMAN on network aspects of heat transfer intensification Task 2.1. Heat transfer enhancement for the tube-side of heat exchangers Task 2.2. Heat transfer enhancement for the shell-side of heat Collaboration with EMbaffle, UNIBATH, UNIMAN on network aspects of heat transfer intensification

5. PIL in WP4 Task 4.1. Development of a streamlined and computationally efficient methodology for design of HENs – work started Collaboration with UNIPAN on incorporation of P-graph and Accelerated Branch-and-Bound algorithms for HEN retrofit Task 4.2. A systematic retrofit procedure will be developed to account for heat exchanger networks prone to fouling deposition The main focus of the workpackage is on retrofit of HEN with intensified heat transfer and fouling mitigation Task 4.3. Development of a software tool Discussions on dll modules structure have started

6. PIL in WP7 Task 7.1 – Overall management of the project and risk contingency planning Task 7.2 – Formal administration responsibilities of the Coordinator within the project gathering of deliverables, submission of reports to the system, etc Task 7.3 – General tasks through the project for the Coordinator (finance, project quality assurance, website

7. Collaborating with UNIMAN and Cal Gavin on the development of intensified heat transfer Modelling of twisted-tape inserts Modelling of coil-wire inserts Modelling of hiTRAN ® Modelling of helical baffles

8. Collaborating with UNIMAN on the methodology of HEN retrofit with intensified heat transfer 9521 kW 6054 kW S1 S2 S3 H 4 495.6K 5 5 3 616K 540K 400K 538K 432K 408.8K 432 K 432.1K 427K 2 2 S4 S5 363K C1 C2 391K 4 1 1 3 F x = 0.1819 F x = 0.6811 299K 379.8K 350K 1268 kW 353 K Total △ P = 233.0 kPa Total △ P = 91.0 kPa Total △ P = 111.1 kPa Total △ P = 34.7 kPa Total △ P = 64.9 kPa By pass (F x ) = 0.3056 13053 kW 9441 kW S1 S2 S3 H 4 478.7K 5 5 3 616K 540K 400K 538K 432K 419.1K 439.3K 449.2K 411.9K 2 2 S4 S5 363K C1 C2 391K 4 1 1 3 F x = 0.1817 F x = 0.6276 299K 394.9K 350K 1420 kW 353 K Total △ P = 101.5 kPa Total △ P = 73.6 kPa Total △ P = 48.1 kPa Total △ P = 20.1 kPa Total △ P = 67.0 kPa

9.  Improving optimal model for HEN retrofit More details for enhancements Large scale problems Minimizing retrofitting costs  Build up optimal model for HEN design Exchanger geometry details Pressure drop constraints Maximizing total profit Working on Requires further collaboration with Cal Gavin, SODRU, UNIMAN, UNIBATH, EMbaffle