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What are the needs for Process Intensification?

Oil & gas science and technology, 2015-03, Vol.70 (3), p.463-473

2015

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Intensification of waste cooking oil transformation by transesterification and esterification reactions in oscillatory baffled and microstructured reactors for biodiesel production

Green processing and synthesis, 2014-12, Vol.3 (6), p.419-429

2014

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Impact of the material on the thermal behaviour of heat exchangers-reactors

Chemical engineering and processing, 2012-02, Vol.52, p.102-111

2012

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Continuous lipase esterification using process intensification technologies

Journal of chemical technology and biotechnology (1986), 2014-10, Vol.89 (10), p.1590-1598

2014

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Flow photochemistry: a meso-scale reactor for industrial applications

Chimica oggi, 2015-09, Vol.33 (5), p.58-62

2015

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Evaluation of an intensified continuous heat-exchanger reactor for inherently safer characteristics

Journal of loss prevention in the process industries, 2008-09, Vol.21 (5), p.528-536

2008

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Two-phase enzymatic reaction using Process Intensification technologies

Chimica oggi, 2013-11, Vol.31 (6), p.43-46

2013

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Pre-Design of a Continuous Intensified Reactor Based on Pure Thermo-Chemical Optimisation

Chemical product and process modeling, 2008-08, Vol.3 (1)

2008

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Dynamic behaviour of a continuous heat exchanger/reactor after flow failure

International journal of chemical reactor engineering, 2008, Vol.6 (article A23)

2008

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Dynamic Behaviour of a Continuous Heat Exchanger/Reactor after Flow Failure

International journal of chemical reactor engineering, 2008-01, Vol.6 (1)

2008

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Intensification of Ester Production in a Continuous Reactor

International journal of chemical reactor engineering, 2009-07, Vol.7 (1), p.1592-1592

2009

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Dynamic Behaviour of a Continuous Heat Exchanger/Reactor after Flow Failure

International journal of chemical reactor engineering, 2008-02, Vol.6 (1), p.1669-1669

2008

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Optimisation of solvent replacement procedures according to economic and environmental criteria

Chemical engineering journal (Lausanne, Switzerland : 1996), 2006-04, Vol.117 (2), p.169-177

2006

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Pre-Design of a Continuous Intensified Reactor Based on Pure Thermo-Chemical Optimisation

Chemical product and process modeling, 2008-08, Vol.3 (1), p.1177-1177

2008

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Performance Evaluation of a Novel Concept "Open Plate Reactor" Applied to Highly Exothermic Reactions

Chemical engineering & technology, 2005-09, Vol.28 (9), p.1028-1034

2005

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Sensor placement and fault detection using an efficient fuzzy feature selection approach

49th IEEE Conference on Decision and Control (CDC), 2010, p.6827-6832

2010

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Dynamic models for start-up operations of batch distillation columns with experimental validation

Computers & chemical engineering, 2004-11, Vol.28 (12), p.2735-2747

2004

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Optimisation of solvent replacement procedures according to economic and environmental criteria in pharmaceutical industry

Chemical engineering journal (Lausanne, Switzerland : 1996), 2006, Vol.1 (2), p.169-177

2006

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Selection of Sensors by a New Methodology Coupling a Classification Technique and Entropy Criteria

Chemical engineering research & design, 2007, Vol.85 (6), p.825-838

2007

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Influence of solvent choice on the optimisation of a reaction–separation operation: application to a Beckmann rearrangement reaction

Separation and purification technology, 2004, Vol.34 (1), p.273-281

2004

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Optimisation of operating conditions in batch for more sustainable continuous process transposition

Chemical product and process modeling, 2008, Vol.3 (1)

2008

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LED-driven spiral-shaped microreactor as a tool to investigate sensitized photooxygenations

EPA newsletter, 2017-11

2017

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Integrated continuous-flow photooxygenation process with solid-supported sensitizers for the safe and sustainable production of fine chemicals and pharmaceuticals (PICPOSS)

EPA newsletter, 2017, p.15-21

2017

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Optimisation of a methyl acetate production process by reactive batch distillation

Computer Aided Chemical Engineering, 2002, Vol.10, p.475-480

2002

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Optimisation of global pharmaceutical syntheses integrating environmental aspects

Computer Aided Chemical Engineering, 2001, Vol.9, p.1127-1132

2001

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What are the needs for Process Intensification?

Intensification of waste cooking oil transformation by transesterification and esterification reactions in oscillatory baffled and microstructured reactors for biodiesel production

Impact of the material on the thermal behaviour of heat exchangers-reactors

Continuous lipase esterification using process intensification technologies

Flow photochemistry: a meso-scale reactor for industrial applications

Evaluation of an intensified continuous heat-exchanger reactor for inherently safer characteristics

Two-phase enzymatic reaction using Process Intensification technologies

Pre-Design of a Continuous Intensified Reactor Based on Pure Thermo-Chemical Optimisation

Dynamic behaviour of a continuous heat exchanger/reactor after flow failure

Dynamic Behaviour of a Continuous Heat Exchanger/Reactor after Flow Failure

Intensification of Ester Production in a Continuous Reactor

Dynamic Behaviour of a Continuous Heat Exchanger/Reactor after Flow Failure

Optimisation of solvent replacement procedures according to economic and environmental criteria

Pre-Design of a Continuous Intensified Reactor Based on Pure Thermo-Chemical Optimisation

Performance Evaluation of a Novel Concept "Open Plate Reactor" Applied to Highly Exothermic Reactions

Sensor placement and fault detection using an efficient fuzzy feature selection approach

Dynamic models for start-up operations of batch distillation columns with experimental validation

Optimisation of solvent replacement procedures according to economic and environmental criteria in pharmaceutical industry

Selection of Sensors by a New Methodology Coupling a Classification Technique and Entropy Criteria

Influence of solvent choice on the optimisation of a reaction–separation operation: application to a Beckmann rearrangement reaction

Optimisation of operating conditions in batch for more sustainable continuous process transposition

LED-driven spiral-shaped microreactor as a tool to investigate sensitized photooxygenations

Integrated continuous-flow photooxygenation process with solid-supported sensitizers for the safe and sustainable production of fine chemicals and pharmaceuticals (PICPOSS)

Optimisation of a methyl acetate production process by reactive batch distillation

Optimisation of global pharmaceutical syntheses integrating environmental aspects

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