کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
6451750 1361374 2016 12 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Downstream separation of poly(hydroxyalkanoates) using crude enzyme consortia produced via solid state fermentation integrated in a biorefinery concept
ترجمه فارسی عنوان
جداسازی پایین از پلی (هیدروکسی آلکانیاها) با استفاده از کنسرسیوم آنزیمی خام تولید شده از طریق تخمیر جامد یکپارچه در یک مفهوم بیورفینشن
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی بیو مهندسی (مهندسی زیستی)
چکیده انگلیسی


- Recovery of poly(hydroxyalkanoates) by a novel process using crude enzymes.
- The temperature and pH of cell lysis were optimized by experimental design.
- The recovery yield of P(3HB-co-3HV) achieved was higher than 98%.
- The purity of P(3HB-co-3HV) achieved was higher than 96.7%.

Crude enzyme produced via solid state fermentation using the fungal strain Aspergillus oryzae was used to lyse cells of Cupriavidus necator, enabling the recovery of poly(3-hydroxybutyrate-co-3-hydroxyvalerate), P(3HB-co-12 mol% 3HV). A central composite design was employed in order to optimize the temperature and the pH value leading to the highest lysis of C. necator cells (88.9 ± 0.4%) and the optimal hydrolysis of protein contained in bacterial cells. Enzymatic lysis of bacterial cells was also carried out at the optimum temperature and uncontrolled pH value leading to P(3HB-co-12 mol% 3HV) recovery yield and purity of 98% and 96.7%, respectively. The bacterial cell lysate obtained after the separation of P(3HB-co-12 mol% 3HV) granules was evaluated as nutrient-rich supplement together with crude glycerol for the production of poly(3-hydroxybutyrate) in shake flask cultures. This novel downstream separation process could be integrated in a sunflower-based biorefinery reducing the cost of poly(hydroxyalkanoate) recovery and fermentation medium formulation.

137

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Food and Bioproducts Processing - Volume 100, Part A, October 2016, Pages 323-334
نویسندگان
, , , , , , , ,