Method to incorporate energy integration considerations in multiproduct batch processes

1994 ◽  
Vol 18 (11-12) ◽  
pp. 1043-1055 ◽  
Author(s):  
J. Corominas ◽  
A. Espuña ◽  
L. Puigjaner
1993 ◽  
Vol 17 ◽  
pp. S15-S20 ◽  
Author(s):  
J. Corominas ◽  
A. Espuna ◽  
L. Puigjaner

Energies ◽  
2020 ◽  
Vol 13 (10) ◽  
pp. 2532
Author(s):  
Ron-Hendrik Hechelmann ◽  
Jan-Peter Seevers ◽  
Alexander Otte ◽  
Jan Sponer ◽  
Matthias Stark

This study highlights the C O 2 , e -emission reduction potentials and related economic consequences for changing steam generation from fossil to renewable. Seven different utility concepts are developed, including a steam accumulator for load management. Peculiarities for the integration of biogas boilers, biomass-fuelled boilers, electrode steam boilers, biomethane-fuelled solid oxide fuel cells, micro gas turbine, solar energy systems, heat pumps and steam accumulators into a steam system with fluctuating steam demand are explained and the energy balance based models for the simulation study are described. The characteristics of batch processes, start up times and part load efficiency are considered via an annual dynamic simulation. Based on a detailed process analysis and dimensioning of the utilities and the accumulator a comprehensive simulation study is conducted for a pet food processing company having an average steam demand of 18,000 MWh at around 9 bar and 3 t/h. The results show that the highest C O 2 , e -emissions reduction of up to 63% is achieved by the transition to a solid biomass-fuelled boiler system. This leads to an increase of the operating costs by 27.8%.


2005 ◽  
Vol 1 (03) ◽  
pp. 93-98
Author(s):  
V. Rogez ◽  
◽  
H. Roisse ◽  
V. Autier ◽  
X. Guillaud

2020 ◽  
Author(s):  
Tomas Hardwick ◽  
Rossana Cicala ◽  
Nisar Ahmed

<p>Many chiral compounds have become of great interest to the pharmaceutical industry as they possess various biological activities. Concurrently, the concept of “memory of chirality” has been proven as a powerful tool in asymmetric synthesis, while flow chemistry has begun its rise as a new enabling technology to add to the ever increasing arsenal of techniques available to the modern day chemist. Here, we have employed a new simple electrochemical microreactor design to oxidise an L-proline derivative at room temperature in continuous flow. Flow performed in microreactors offers up a number of benefits allowing reactions to be performed in a more convenient and safer manner, and even allow electrochemical reactions to take place without a supporting electrolyte due to a very short interelectrode distance. By the comparison of electrochemical oxidations in batch and flow we have found that continuous flow is able to outperform its batch counterpart, producing a good yield (71%) and a better enantiomeric excess (64%) than batch with a 98% conversion. We have, therefore, provided evidence that continuous flow chemistry has the potential to act as a new enabling technology to replace some aspects of conventional batch processes. </p>


2010 ◽  
Vol 36 (9) ◽  
pp. 1312-1320 ◽  
Author(s):  
Yu-Qing CHANG ◽  
Shu WANG ◽  
Shuai TAN ◽  
Fu-Li WANG ◽  
Jie YANG

Author(s):  
Hannu Huuki ◽  
Santtu Karhinen ◽  
Maria Kopsakangas-Savolainen ◽  
Rauli Svento

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