scholarly journals Effect of interferon on the development of Trypanosoma cruzi in tissue culture "Vero" cells

1980 ◽  
Vol 75 (1-2) ◽  
pp. 157-160 ◽  
Author(s):  
R. R. Golgher ◽  
M. S. M. Bertelli ◽  
M. L. Petrillo-Peixoto ◽  
Z. Brener

Results are presented on the effects of interferon on the intracellular stages of T. cruzi in tissue culture "Vero" cells. Interferon was obtained by infecting monolayers of human amniotic cells with inactivated Newcastle disease virus. Interferon has not affected the cell infection by T. cruzi culture infective stages and neither has it prevented the transformation of amastigote into trypomastigote stages.

2010 ◽  
Vol 2010 ◽  
pp. 1-7 ◽  
Author(s):  
Mohd Azmir Arifin ◽  
Maizirwan Mel ◽  
Mohamed Ismail Abdul Karim ◽  
Aini Ideris

The aim of this study is to prepare a model for the production of Newcastle disease virus (NDV) lentogenic F strain using cell culture in bioreactor for live attenuated vaccine preparation. In this study, firstly we investigated the growth of Vero cells in several culture media. The maximum cell number was yielded by culture of Vero cells in Dulbecco's Modified Eagle Medium (DMEM) which was1.93×106 cells/ml. Secondly Vero cells were grown in two-litre stirred tank bioreactor by using several commercial microcarriers. We achieved the maximum cell concentration about7.95×105 cells/ml when using Cytodex 1. Later we produced Newcastle Disease virus in stirred tank bioreactor based on the design developed using Taguchi L4 method. Results reveal that higher multiplicity of infection (MOI) and size of cell inoculums can yield higher virus titer. Finally, virus samples were purified using high-speed centrifugation based on3∗∗(3-1) Fractional Factorial Design. Statistical analysis showed that the maximum virus titer can be achieved at virus sample concentration of 58.45% (v/v), centrifugation speed of 13729 rpm, and centrifugation time of 4 hours. As a conclusion, high yield of virus titer could be achieved through optimization of cell culture in bioreactor and separation by high-speed centrifugation.


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