Miniplants — Ein Beitrag zur inhärenten Sicherheit?

Behr, Alexander S.; Ebbers, Wolfram; Wiese, N.

doi:10.1002/1522-2640(200010)72:10<1157::aid-cite1157>3.3.co;2-f

Cited by 4 publications

(3 citation statements)

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“…Since this first gathering in Europe, seven IMRET conferences have been organized on an alternate basis by the AIChE in North America ,,, and by DECHEMA in Europe, ,, with the latest one being IMRET-9 . In addition to these conferences, recent progress on microcomponents, microprocesses, and mathematical modeling is described in a number of excellent review articles, − various monographs, ,,,, and in the proceedings of dedicated workshops. − It is also generally agreed that microscale systems represent a definitive methodology for process intensification. , The latter is also consistent with the often-cited advantages of microreaction systems when compared to conventional reactor systems, which include (i) safer operation; (ii) simplified scale-up; (iii) improved heat and mass transfer characteristics; and (iv) application flexibility. ,, …”

Section: Introductionmentioning

confidence: 77%

“…33 Since this first gathering in Europe, seven IMRET conferences have been organized on an alternate basis by the AIChE in North America 34,36,38,40 and by DECHEMA in Europe, 35,37,39 with the latest one being IMRET-9. 41 In addition to these conferences, recent progress on microcomponents, microprocesses, and mathematical modeling is described in a number of excellent review articles, [42][43][44] various monographs, 31,32,42,45,46 and in the proceedings of dedicated workshops. [47][48][49] It is also generally agreed that microscale systems represent a definitive methodology for process intensification.…”

Section: Introductionmentioning

confidence: 99%

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Integrated Microreactor System for Gas-Phase Catalytic Reactions. 1. Scale-up Microreactor Design and Fabrication

and¹,

Jensen²,

Schmidt

et al. 2007

Ind. Eng. Chem. Res.

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The design and fabrication of a gas-phase microreactor that is based upon a multilayer laminate microelectronics structure is described. The reactor is a key component in an integrated system whose platform utilizes a commercial computer chassis with modular boards to perform the required process functions. The design combines knowledge from earlier laminate microstructures with new prototyping concepts for incorporation of various on-board devices. A 3-D finite element simulation model was used to identify various design improvements. The final device contains two parallel reaction channels on a chiplike die in which a 1 μm platinum film catalyst is deposited on the underside of a silicon nitride membrane. Seven platinum heaters and temperature sensors are evenly distributed along the top side of the silicon nitride membrane. Electrical contacts for the on-board control and sensing devices are achieved through various pins that are distributed around the reactor die. The experience and knowledge gained in developing the final reactor device is utilized in Part 2 of this series for reactor packaging and development of the integrated system modules.

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Section: Introductionmentioning

confidence: 77%

Section: Introductionmentioning

confidence: 99%

Integrated Microreactor System for Gas-Phase Catalytic Reactions. 1. Scale-up Microreactor Design and Fabrication

and¹,

Jensen²,

Schmidt

et al. 2007

Ind. Eng. Chem. Res.

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“…Even fully automatic production of sample quantities is feasible. 3,17,[35][36][37][38][39] The present study aimed at the first successful rutheniumcatalyzed hydroformylation in a continuously operated miniplant in order to assess its long-term stability for potential technical applications. To do so, initially the catalytic system developed by Beller et al [21][22][23] had to be optimized on a laboratory scale regarding conversion and selectivity, identifying significant parameters of influence for controlling the reaction.…”

Section: Introductionmentioning

confidence: 99%

Ruthenium-catalyzed hydroformylation: from laboratory to continuous miniplant scale

Kämper

Kucmierczyk

Seidensticker

et al. 2016

Catal. Sci. Technol.

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Process Development, 1. Fundamentals and Standard Course

Vogel

2011

Ullmann's Encyclopedia of Industrial Chemistry

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The article contains sections titled: 1. Introduction 1.1. Objective of Industrial Research and Development 1.2. Production Structure of the Chemical Industry 1.3. Chemical Production Plant and its Components 1.4. The Task of Process Development 2. Course of Process Development 2.1. Process Development as an Iterative Process 2.2. Drawing up an Initial Version of the Process 2.2.1. Data Banks 2.2.2. Simulation Programs 2.2.3. Expert Systems 2.3. Checking Individual Steps 2.4. Testing the Entire Process on a Small Scale 2.4.1. Microplant: Link between Laboratory and Miniplant 2.4.2. Miniplant Technique 2.4.2.1. Introduction 2.4.2.2. Construction 2.4.2.3. Limits of Miniaturization 2.4.2.4. Limitations of the Miniplant Technique 2.4.3. Pilot Plant 3. Planning, Erection and Start‐Up of a Chemical Plant

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Miniplants — Ein Beitrag zur inhärenten Sicherheit?

Cited by 4 publications

References 0 publications

Integrated Microreactor System for Gas-Phase Catalytic Reactions. 1. Scale-up Microreactor Design and Fabrication

Integrated Microreactor System for Gas-Phase Catalytic Reactions. 1. Scale-up Microreactor Design and Fabrication

Ruthenium-catalyzed hydroformylation: from laboratory to continuous miniplant scale

Process Development, 1. Fundamentals and Standard Course

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