Effects of temperature ramp rate during the primary drying process on the properties of amorphous-based lyophilized cake, Part 1: Cake characterization, collapse temperature and drying behavior

2017 ◽  
Vol 39 ◽  
pp. 131-139 ◽  
Author(s):  
Ryo Ohori ◽  
Chikamasa Yamashita
2020 ◽  
Vol 578 ◽  
pp. 119116 ◽  
Author(s):  
Getachew Assegehegn ◽  
Edmundo Brito-de la Fuente ◽  
José M. Franco ◽  
Críspulo Gallegos

Author(s):  
Gardis J.E. Von Gersdorff ◽  
Luna Shrestha ◽  
Sharvari Raut ◽  
Stefanie K. Retz ◽  
Oliver Hensel ◽  
...  

The drying of beef has gained an increasing interest and the organic market shows an increasing demand for dried beef products. In this study, organic beef meat slices were dried at 50 °C, 60 °C and 70 °C. Moisture content and color was measured throughout the drying process alongside Vis/VNIR hyperspectral images of the slices. The results of the total color difference (ΔE) showed the biggest change for samples dried at 50 °C (ΔE = 25.6). The aw value was the lowest for slices dried at 50 °C (0.744). The hyperspectral data gave promising results regarding non-invasive prediction of moisture content and color. Keywords: beef drying; drying behavior;color; hyperspectral imaging; quality.  


2020 ◽  
Vol 38 (1) ◽  
pp. 93-98
Author(s):  
Gustavo Soares Wenneck ◽  
Reni Saath ◽  
Roberto Rezende ◽  
Juliana Parisotto Poletine ◽  
Danilo César Santi ◽  
...  

Author(s):  
Thomas W. Secord ◽  
Susan C. Mantell ◽  
Kim A. Stelson

In thermosetting composite manufacturing, part thickness, mold temperature, pressure, and resin kinetics can affect the uniformity of cure in the finished part. If the interaction of these parameters is not accounted for, then unwanted overshoot of the processing temperature can occur within a part during cure. In this paper, the relationship between processing and material parameters was considered to establish a critical thickness separating parts having large overshoots from parts having small overshoots. The one-dimensional heat equation with an autocatalytic relation for curing was used to model the process. The equations were placed in dimensionless form using a scaling analysis. A finite difference model was also created to calculate part temperatures during cure as a function of the key dimensionless groups. For experimental validation, composite plates of varying thickness were fabricated from a glass fiber prepreg material, and the processing conditions were varied according to thickness. The scaling analysis identified five dimensionless groups. Two of these groups were found to affect the overshoot of the temperature: the modified Damköhler number Da∗, which includes the heat generated during the reaction, and the dimensionless temperature ramp rate t¯rise, which describes the tooling temperature ramp rate relative to the natural time scale of the heat transfer. There was good agreement between the numerical model prediction of temperature overshoot and the experimental data. The results also confirm that the behavior of thin and thick parts, as defined by the relative temperature overshoot, can be well defined and predicted by the two proposed dimensionless groups: Da∗ and t¯rise.


1984 ◽  
Vol 36 ◽  
Author(s):  
R. F. Pinizzotto ◽  
H. F. Schaake ◽  
R. G. Massey ◽  
D. W. Heidt

ABSTRACTA new method for the nucleation of oxygen precipitates in Czochralski silicon is described. The temperature is ramped at approximately 100°C/hr from a very low value, near 400°C, to the highest temperature used for subsequent process steps. The technique generates a larger precipitate number density and a greater volume fraction of precipitated oxygen than standard isothermal nucleation anneals. The morphology of the precipitates changes from 0.lum sizéd (100) platelets to small particles unresovable by TEM. The new temperature ramping technique can reduce the time needed for precipitate nucleation by at least a factor of three. The details of oxygen precipitation can be totally controlled by adjusting the temperature ramp rate as a function of time.


1999 ◽  
Vol 85 (5) ◽  
pp. 2617-2626 ◽  
Author(s):  
S.-L. Zhang ◽  
C. Lavoie ◽  
C. Cabral ◽  
J. M. E. Harper ◽  
F. M. d’Heurle ◽  
...  

2010 ◽  
Vol 5 (1) ◽  
Author(s):  
Zia ul- Islam ◽  
Ramdhane Dhib ◽  
Yaser Dahman

This work presents the dynamic modeling of drying behavior of polymer solutions in an infrared-convective oven. Two study cases were considered for the drying process. The first one deals with the drying of a coated polymer solution on a fixed substrate while the second one includes drying of the same solution on a moving substrate in an infrared (IR) oven. Both models involve simultaneous heat and mass transfer equations that describe changes in the solvent concentration and the polymer temperature during the drying process. The set of partial differential equations (PDEs) arising from the mass and energy balances constitute a highly nonlinear system due to inter-dependence of the thermodynamic and transport properties of polymer solutions. The models were numerically solved and were validated using published experimental data. The models were employed to simulate the drying of a polyvinyl acetate coating (in toluene) on a polyester substrate. Results obtained from the derived model demonstrated the importance of parameters such as web velocity, heater temperature, and inlet air velocity in the IR drying process. In general, high temperature and air velocity cause rapid drying of the polymer coating, while high substrate velocity resulted in drying. This model can be applied on any industrial applications that include continuous IR drying process of polymer-coated layers to predict the drying behavior of the coated product.


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