Team:UCL London/Economic Evaluation
From 2010.igem.org
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So using 0.1 mM, how much IPTG you need in grams: 0.1 mM * (1M/1000mM) = 0.0001 M | So using 0.1 mM, how much IPTG you need in grams: 0.1 mM * (1M/1000mM) = 0.0001 M | ||
- | 238.3 g/M * (0.0001 M) = 0.02383 grams<<< this is how many grams of IPTG you need per a kg of a feedstream. | + | 238.3 g/M * (0.0001 M) = 0.02383 grams<<< |
+ | this is how many grams of IPTG you need per a kg of a feedstream. | ||
Finally for a 1,000 L fermentation batch | Finally for a 1,000 L fermentation batch |
Revision as of 22:59, 22 October 2010
Economic Evaluation
Estimate of IPTG cost for an industrial scale fermentation - say 1000L
From Sigma Aldrich (readily available): Isopropyl-Beta-D-thiogalactopyranoside (IPTG) solution costs £32.30p for 200 mM IPTG
IPTG’s molar mass= 238.3 g/M
200* (1 M/ 1000 mM) = 0.2 M 0.2 M * (238.3 g/M) = 47.66 g
So its £32.30p for 47.66 grams, therefore £ 0.68 pence /gram
From literature: 0.1 mM (This value is usually used for a high FAb production)
So using 0.1 mM, how much IPTG you need in grams: 0.1 mM * (1M/1000mM) = 0.0001 M
238.3 g/M * (0.0001 M) = 0.02383 grams<<< this is how many grams of IPTG you need per a kg of a feedstream.
Finally for a 1,000 L fermentation batch
Using SuperPro Designer you can assume kg = L
So for 1,000 kg/batch, this is how much IPTG you need:
1,000 * 0.02383 g * (1 kg/ 1,000 g) = 0.02383 kg /batch
Cost of IPTG per a batch:
0.02383 (kg/batch) * 0.6777 (£/ gram) * (1,000 gram / 1 kg) = £ 16. 15 p / batch
Advantages and Disadvantages of Auto-Induction
Advantages
• Simple procedure, expression strain inoculated in the auto-inducing media
- No holding tank required for IPTG, therefore cost saving in equipment costs (Note: lowering the equipment costs, also lowers the capital investment)
- And maybe a slight reduction in CIP and SIP costs
• High titres achieved when auto-inducing compared to using IPTG
- Reduces size of fermenter required (as there is more target protein per volume of culture), which lowers the USP equipment costs.
- Also number of batches produced per a year would be less
Disadvantages
• Auto-induction uses complex medium
- Complex medium, more expensive
- Could increase the Cost of Goods (COG’s), dependent on the prices of IPTG and complex media.
• At high titres, nature of the feedstream has an impact on the purification steps
- Protein A resin required to capture more product
- High titres bring about more impurities, purification steps may struggle to remove this higher level of impurities.
- Resin lifetime reduces due to fouling, therefore more resin required
- Protein A resin expensive and a significant cost driver for DSP costs
• Possibility of unintended induction
- Could potentially kill cells and produce unexpected impurities that cannot be removed downstream or require further purification steps
• Cultures grown using auto-inducing media may not be suitable as frozen stocks.
- Limited time for use
- Potential risk; loss of stocks due to decrease in viability