Extraction of diosgenin from hydrolysate in an extraction device with a rotary film evaporator

1983 ◽  
Vol 17 (5) ◽  
pp. 371-374
Author(s):  
M. I. Lakoza ◽  
V. V. Panina ◽  
V. S. Gershanovskii ◽  
L. G. Zelinskaya ◽  
A. M. Poznyak
Keyword(s):  
Film Evaporator ◽  
Extraction Device ◽  
Rotary Film

A simple, inexpensive rotary film evaporator

1960 ◽  
Vol 37 (5) ◽  
pp. 247
Author(s):  
Edward M. Arnett
Keyword(s):  
Film Evaporator ◽  
Rotary Film

scholarly journals Determination of heat transfer coefficient in advanced rotary film evaporator

2021 ◽  
Vol 4 (3(60)) ◽  
pp. 42-45
Author(s):  
Aleksey Zagorulko ◽  
Andrii Zahorulko ◽  
Maksym Serik ◽  
Vyacheslav Оnishchenko ◽  
Alexander Postadzhiev
Keyword(s):  
Heat Transfer ◽  
Heat Transfer Coefficient ◽  
Transfer Coefficient ◽  
Flow Rate ◽  
Fruit And Vegetable ◽  
Important Indicator ◽  
Periodic Action ◽  
Film Evaporator ◽  
Rotary Film ◽  
The Heat Transfer Coefficient

The object of research is the process of concentrating fruit and vegetable purees in an improved rotary film evaporator. The existing hardware design of traditional processes for processing fruits and vegetables, as a rule, is not unified enough, inconvenient in operation and is designed for high productivity. Concentration of fruit and vegetable purees occurs mainly in vacuum evaporators of periodic and continuous operation at a temperature of 60–80 °C under vacuum, which allows them to significantly preserve their nutritional value. But the duration of the process remains very significant (in devices of periodic action up to 75–90 minutes). One of the most problematic areas in the concentration of fruit and vegetable raw materials is significant losses of biologically active substances. At the same time, an important indicator of the quality of the process of concentrating pasty fruit and vegetable pastes is the value of the heat transfer coefficient, which characterizes the efficiency of the heat transfer method and the design features of the mixing device, taking into account the thermophysical characteristics of the product. To create conditions for conducting research to determine the heat transfer coefficient, it is necessary to use instrumentation with precise regulation of the necessary technological parameters. To study the heat transfer coefficient when concentrating fruit and vegetable purees, an automatic installation of an improved rotary evaporator was designed. The improvement of the rotary film evaporator (RFE) is carried out due to the lower location of the separating space by installing a screw discharge of the paste and preheating the output puree with secondary steam. The experimental dependences of the heat transfer coefficient on the product flow rate make it possible to determine the rational values of the flow rate of the RFE feedstock at various values of the rotor shaft speed. It is found that the heat transfer coefficient is influenced to a large extent by the product consumption, and the rotor speed acts to a lesser extent, only the relative speed of fluid passage around the developed hinged blade changes. It is found that when the frequency changes from 0.3 to 1.7 s–1, an increase in the heat transfer coefficient by 1.45 times is observed, which is explained by a more intensive degree of mixing of the product by the blades.

Analysis of the interconnection of parameters in a rotary film evaporator

1978 ◽  
Vol 12 (9) ◽  
pp. 1227-1231
Author(s):  
O. A. Krechetova ◽  
Yu. G. Lakeev ◽  
L. P. Losev ◽  
G. V. Mel'nikova
Keyword(s):  
Film Evaporator ◽  
Rotary Film

scholarly journals Investigation dehydration process microbiological materials in a rotary-film evaporator

2013 ◽  
Vol 6 (8(66)) ◽  
pp. 36
Author(s):  
Олександр Миколайович Ободович ◽  
Сергій Ігорович Костик
Keyword(s):  
Dehydration Process ◽  
Film Evaporator ◽  
Rotary Film

scholarly journals Determination of the heat transfer coefficient of a rotary film evaporator with a heating film-forming element

2021 ◽  
Vol 6 (8 (114)) ◽  
Author(s):  
Andrii Zahorulko ◽  
Aleksey Zagorulko ◽  
Oleksander Cherevko ◽  
Olena Dromenko ◽  
Alla Solomon ◽  
...  
Keyword(s):  
Heat Transfer ◽  
Heat Transfer Coefficient ◽  
Heated Surface ◽  
Raw Material ◽  
Film Evaporator ◽  
Reflective Surface ◽  
Film Forming ◽  
Criterion Equation ◽  
Rotary Film ◽  
The Heat Transfer Coefficient

A model of a rotary film evaporator with a film-forming element with a reflective heated surface has been developed. This will allow stabilizing the hydraulic movement of the cut wave flow due to the reflective surface of the geometric shape for the forced direction of the cut raw material to the heating surface. Autonomous heating of the reflective surface additionally provides a temperature effect in the conditions of movement of particles of raw materials after cutting. The analysis of the experimental and theoretical parameters of heat transfer made it possible to substantiate the criterion equation for determining the heat transfer coefficient of an evaporator with the proposed film-forming element and a reflective heated surface for calculating the coefficient from the working surface to the raw material. The resulting equation takes into account the influence of the vertical component of the motion of the raw material film, centrifugal movement during the rotation of the film-forming element, mixing of the boiling film of the raw material with steam bubbles, and the geometric characteristics of the film-forming blade on the hydrodynamic flow of the raw material. The calculation of the rotary-film evaporator was carried out using the criterion equation and the obtained useful heat exchange surface – 0.75 m2. The specific metal consumption in a rotary film evaporator with a film-forming element having a reflective surface is 57 kg/m2, compared to the vacuum evaporator traditionally used in canning industries (410 kg/m2), which is 7.1 times less. The duration of the temperature effect on the raw material is also reduced: a rotary film evaporator – 200 s and 3600 s in a traditional apparatus. The data obtained will be useful for the design of rotary-film devices of different geometric parameters using articulated blades with a reflective plate.

A simple rotary film evaporator

1956 ◽  
Vol 33 (11) ◽  
pp. 446-447
Author(s):  
B B Marsh ◽  
P M Nottingham
Keyword(s):  
Film Evaporator ◽  
Rotary Film

All-Glass Rotary Film Evaporator

1955 ◽  
Vol 27 (7) ◽  
pp. 1207-1207 ◽  
Author(s):  
M. E. Volk
Keyword(s):  
Film Evaporator ◽  
Rotary Film
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