continuous vacuum
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Processes ◽  
2021 ◽  
Vol 9 (12) ◽  
pp. 2187
Author(s):  
Claas Steenweg ◽  
Anne Cathrine Kufner ◽  
Jonas Habicht ◽  
Kerstin Wohlgemuth

Integrated continuous manufacturing processes of active pharmaceutical ingredients (API) provide key benefits concerning product quality control, scale-up capability, and a reduced time-to-market. Thereby, the crystallization step, which is used in approximately 90% of API productions, mainly defines the final API properties. This study focuses on the design and operation of an integrated small-scale process combining a continuous slug flow crystallizer (SFC) with continuous particle isolation using the modular continuous vacuum screw filter (CVSF). By selective adjustment of supersaturation and undersaturation, the otherwise usual blocking could be successfully avoided in both apparatuses. It was shown that, during crystallization in an SFC, a significant crystal growth of particles (Δd50,3≈ 220 µm) is achieved, and that, during product isolation in the CVSF, the overall particle size distribution (PSD) is maintained. The residual moistures for the integrated process ranged around 2% during all experiments performed, ensuring free-flowing particles at the CVSF outlet. In summary, the integrated setup offers unique features, such as its enhanced product quality control and fast start-up behavior, providing a promising concept for integrated continuous primary manufacturing processes of APIs.


Author(s):  
N. G. Kulneva ◽  
V. A. Fedoruk ◽  
N. A. Matvienko ◽  
E. M. Ponomareva

The article discusses the concepts of continuous vacuum apparatus operation: vertical VKT (VKT – Verdampfungs-Kristallisations-Turm) and horizontal cascade of VKH vacuum apparatus (VKH —horizontal vacuum pan) from BMA (Germany). The advantages and features of the vertical continuous vacuum apparatus VKT are shown, as well as the possibilities for increasing the efficiency of the product department of sugar factories. Thanks to the special design of the crystallization chambers, the low massecuite level above the heating chamber and the use of mechanical stirrers in each chamber, the VKT apparatus can operate without difficulty with a very small temperature difference between heating steam and massecuite, as well as with an absolute heating steam pressure well below 1 bar. With optimal use of VKT vacuum apparatus, a variety of energy-saving schemes can be implemented, for example, double-effect evaporation in the crystallization section. Part of the secondary crystallization steam is used to heat one of the VKT units, which saves the heating steam of the evaporator unit used for this purpose. With an increase in the productivity of the sugar factory, it is possible to quickly equip the VKT apparatus with an additional chamber. The device works continuously throughout the season, especially with products with massecuite purity of more than 94%. The chambers are cleaned without stopping the entire apparatus. The boiling of massecuite of all stages of crystallization in VKT devices ensures a uniform operating mode of the food compartment, allows to achieve an increase in sugar yield and helps to reduce steam consumption at the plant.


Author(s):  
Jose Jonathan Rubio Arias ◽  
Jinsang Kim ◽  
Bianca Pedroso Silva Santos ◽  
Lais Schmidt Albuquerque ◽  
Isabela Custodio Mota ◽  
...  

2020 ◽  
pp. 288-293
Author(s):  
A. Goyal ◽  
D. Kumar ◽  
D. Mishra ◽  
S. Awasthi

Crystallization is a key section of sugar manufacture for controlling the sugar quality as well as energy consumption. In this paper, i-VCP, a new vertical continuous evaporating crystallizer (vacuum pan) design is described. Unlike some other VCPs, i-VCP has a partitioned shell in the top compartments especially for low-grade massecuites, which helps to keep coefficient of variation at 25–30% and about a vapor consumption of about 28 kg/100 kg massecuite. A high vapor space avoids entrainment and efficient mechanical circulators with variable frequency drives reduce power consumption. Flexibility to use different pressure vapors in different compartments and an inbuilt seed magma crystallizing compartment obviate the demand for a separate batch apparatus. One 100t/h capacity A massecuite i-VCP installed at Dalmia Bharat Sugar Ltd. (India) and one 25t/h capacity B or C massecuite i-VCP have completed their first season without any stoppages.


2020 ◽  
Vol 61 (3) ◽  
pp. 195-201
Author(s):  
Joachim Lahiani ◽  
Gert W. Niebauer
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