ÇALIK, P. Et Al. 2018. Hybrid fed-batch bioreactor operation design: control of substrate uptake enhances recombinant protein production in high-cell-density fermentations. JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY , vol.93, no.11 , 3326-3335.

ÇALIK, P., Hoxha, B., ÇALIK GARCİA, G., & Ozdamar, T. H., (2018). Hybrid fed-batch bioreactor operation design: control of substrate uptake enhances recombinant protein production in high-cell-density fermentations. JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY , vol.93, no.11, 3326-3335.

ÇALIK, PINAR Et Al. "Hybrid fed-batch bioreactor operation design: control of substrate uptake enhances recombinant protein production in high-cell-density fermentations," JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY , vol.93, no.11, 3326-3335, 2018

ÇALIK, PINAR Et Al. "Hybrid fed-batch bioreactor operation design: control of substrate uptake enhances recombinant protein production in high-cell-density fermentations." JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY , vol.93, no.11, pp.3326-3335, 2018

ÇALIK, P. Et Al. (2018) . "Hybrid fed-batch bioreactor operation design: control of substrate uptake enhances recombinant protein production in high-cell-density fermentations." JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY , vol.93, no.11, pp.3326-3335.

@article{article, author={PINAR ÇALIK Et Al. }, title={Hybrid fed-batch bioreactor operation design: control of substrate uptake enhances recombinant protein production in high-cell-density fermentations}, journal={JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY}, year=2018, pages={3326-3335} }