Design and scale-up of continuous di-nitration reaction using pinched tube flow reactor

Author(s):  
Arshad Hussain ◽  
Mrityunjay Sharma ◽  
Suneha Patil ◽  
Roopashree B. Acharya ◽  
Mahesh Kute ◽  
...  
Keyword(s):  
Scale Up ◽  
Processes ◽  
2021 ◽  
Vol 9 (3) ◽  
pp. 464
Author(s):  
Xingren Jiang ◽  
Ning Yang ◽  
Rijie Wang

Continuous manufacturing has received increasing interest because of the advantages of intrinsic safety and enhanced mass transfer in the pharmaceutical industry. However, the difficulty for scale-up has limited the application of continuous manufacturing for a long time. Recently, the tubular flow reactor equipped with the Kenics static mixer appears to be a solution for the continuous process scale-up. Although many influence factors on the mixing performance in the Kenics static mixer have been investigated, little research has been carried out on the aspect ratio. In this study, we used the coefficient of variation as the mixing evaluation index to investigate the effect of the aspect ratio (0.2–2) on the Kenics static mixer’s mixing performance. The results indicate that a low aspect ratio helps obtain a shorter mixing time and mixer length. This study suggests that adjusting the aspect ratio of the Kenics static mixer can be a new strategy for the scale-up of a continuous process in the pharmaceutical industry.


Author(s):  
Kelsey Fournier ◽  
Nancy Marina ◽  
Neeraj Joshi ◽  
Vincent R. Berthiaume ◽  
Sara Currie ◽  
...  

Fuel ◽  
1988 ◽  
Vol 67 (3) ◽  
pp. 334-340 ◽  
Author(s):  
Odolphus S.L. Bruinsma ◽  
Peter J.J. Tromp ◽  
Henry J.J. de Sauvage Nolting ◽  
Jacob A. Moulijn

2017 ◽  
Vol 13 ◽  
pp. 120-126 ◽  
Author(s):  
Christian H Hornung ◽  
Miguel Á Álvarez-Diéguez ◽  
Thomas M Kohl ◽  
John Tsanaktsidis

This work describes the Diels–Alder reaction of the naturally occurring substituted butadiene, myrcene, with a range of different naturally occurring and synthetic dienophiles. The synthesis of the Diels–Alder adduct from myrcene and acrylic acid, containing surfactant properties, was scaled-up in a plate-type continuous-flow reactor with a volume of 105 mL to a throughput of 2.79 kg of the final product per day. This continuous-flow approach provides a facile alternative scale-up route to conventional batch processing, and it helps to intensify the synthesis protocol by applying higher reaction temperatures and shorter reaction times.


2004 ◽  
Vol 49 (4) ◽  
pp. 13-18 ◽  
Author(s):  
C.S. Zalazar ◽  
M.D. Labas ◽  
C.A. Martín ◽  
R.J. Brandi ◽  
A.E. Cassano

A procedure to scale-up photoreactors employed in AOPs using laboratory information has been developed. Operating with a model compound the proposed procedure was applied to the decomposition of formic acid in water solution using hydrogen peroxide and UV radiation. With laboratory experiments the parameters of the kinetic equation were obtained in a small batch reactor operated within a recycling apparatus. The whole system was modeled employing radiation and mass balances. These balances were used together with a non-linear parameter estimator to derive the model kinetic constants. Then, these results were used in the modeling of the large-scale reactor to predict exit conversions in an isothermal, continuous, tubular flow reactor that is 2 m long and has a volume of 12 l. Once more, radiation and mass balances were used to predict formic acid output concentrations. Experimental data in the large-scale apparatus are in good agreement with theoretical predictions.


2020 ◽  
Vol 10 (3) ◽  
pp. 1080 ◽  
Author(s):  
Qian Yu ◽  
Wim Brilman

Direct air capture (DAC) of CO2 can address CO2 emissions from distributed sources and produce CO2 from air virtually anywhere that it is needed. In this paper, the performance of a new radial flow reactor (RFR) for CO2 adsorption from ambient air is reported. The reactor uses a supported amine sorbent and is operated in a batch mode of operation or semi-continuously, respectively without or with sorbent circulation. The radial flow reactor, containing 2 kg of the adsorbent, is successfully scaled up from the experimental results obtained with a fixed bed reactor using only 1 g of the adsorbent. In the batch operation mode, the sorbent in the annular space of the RFR is regenerated in situ. With sorbent circulation, the RFR is loaded and unloaded batchwise and only used as an adsorber. A sorbent batch loaded with CO2 is transported to and regenerated in an external (fluid bed) regenerator. The RFR unit is characterized by a low contacting energy (0.7–1.5 GJ/ton-CO2) and a relatively short adsorption time (24–43 min) compared to other DAC processes using the same types of sorbents. The contactor concept is ready for further scale-up and continuous application.


Fuel ◽  
1988 ◽  
Vol 67 (3) ◽  
pp. 327-333 ◽  
Author(s):  
Odolphus S.L. Bruinsma ◽  
Rob S. Geertsma ◽  
Pim Bank ◽  
Jacob A. Moulijn

2018 ◽  
Vol 16 (41) ◽  
pp. 7568-7573 ◽  
Author(s):  
Joshua P. Barham ◽  
Souma Tamaoki ◽  
Hiromichi Egami ◽  
Noriyuki Ohneda ◽  
Tadashi Okamoto ◽  
...  

C-Alkylation of N-alkylamides with styrenes is reported, proceeding in ambient air/moisture to give arylbutanamides and other pharmaceutically-relevant scaffolds in excellent mass balance.


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