Team:UCL London/Doxycycline

From 2010.igem.org

(Difference between revisions)
(Doxycycline Biorocess Flowsheet)
(Doxycycline Biorocess Flowsheet)
 
Line 16: Line 16:
Cost of Doxycycline per a batch:
Cost of Doxycycline per a batch:
12 (gram/batch) * 32.20 ($ / gram) = $386.40 per a 1,000 batch
12 (gram/batch) * 32.20 ($ / gram) = $386.40 per a 1,000 batch
 +
'''Bioprocess Flowsheet'''
'''Bioprocess Flowsheet'''

Latest revision as of 16:20, 27 October 2010

UCL IGEM 2010

RETURN TO IGEM 2010

Doxycycline Economic Analysis

Doxycycline Biorocess Flowsheet

Cost

Estimate of Doxycycline cost for an industrial scale fermentation based on the 1,000L mammalian cell model


From Sigma Aldrich website for Doxycycline hyclate cost is $ 32.20 for 1 gram of Doxycycline

Finally for a 1,000 L fermentation batch, this is how much Doxycycline you need is 0.012 kg per 1,000 L batch

Cost of Doxycycline per a batch: 12 (gram/batch) * 32.20 ($ / gram) = $386.40 per a 1,000 batch


Bioprocess Flowsheet

A bioprocess flowsheet was constructed with regards to the mammalian cell system, in order to define all the necessary upstream and downstream steps and assess whether this choice is a feasible one.

The main steps for the antibody production expressed in mammalian cell culture are the primary recovery, primary purification, viral inactivation, secondary purification and viral exclusion prior to formulation, as indicated by the following SuperPro flowsheet.

Ucl-doxylcien.png

Mammalian cell process using Doxycline

Production Volume (L) Titre (g/L) Product Generated (kg/batch) Annual Production (kg/yr) Batches (per a year) Centrifugation Yield (%) Filtration Yield (%) Purification Yield (%) Overall Yield (%) No. Bioreactors Scale of Bioreactors (L)
40,00026.3132.42194100706717000

Note: 7,000 L fermenter example

Executive Summary

Capital Investment ($) 42,013,000
Operating Costs ($/yr)16,210,726
Product Unit Cost ($/kg)122,475
Labour Cost ($/yr)1,805,307

After removing Doxycline from the production process

' Before After
Capital Investment ($)42,013,00041,820,000
Operating costs ($/yr)16,210,72616,153,925
Cogs ($/g)122.5122.1

Annual Operating Cost

Annual Operating Cost ' '
Cost Item$%
Raw Materials5,477,72634
Labour-Dependent1,805,00011
Facility-Dependent6,050,00037
Laboratory/QC/QA903,0006
Consumables1,966,00012
Wste Treatment/Disposable6,0000.0
Utilities3,0000.0
Total16,210,726100
Cogs ($/g)122.47

Could this be because of Doxycline? No, doxycline makes up only 1% of the total raw material costs

Material Cost

Material Costs Unit Cost ($/kg) Annual Amount (kg) Annual Cost ($) %
Media300164,8600.088722951
SerumFree Media30017,1845,155,16994.11148327
Doxycline322001.76456,8011.03694128
Water033500
WFI0.15517,65077,6471.417504323
Air088,69400
H3PO4 (5% w/w)0.14121,07117,2530.314966478
NaOH (0.5M)0.2599,04224,2710.44308534
Protein A Equil 0.15144,25122,0630.402776641
Protein A Eluti0.1565,34710,0290.18308693
Prot- A Reg Buffer0.1739,2306,5800.120122844
NaOH (0.1M)0.24135,79933,0150.60271363
IEX -Eq-Buffer0.1921,4914,0000.073023005
IEX-Wash-Buffer0.2221,5864,7660.087006911
IEX-El-Buffer0.351,2174230.007722183
NaCl (1M)0.3713,1964,8600.088722951
Amm. Sulfate89197,3540.134252795
HIC-Eq-Buffer0.918,5227,7440.141372538
HIC-Wash-Buffer0.5420,25610,8980.198951178
HIC-El-Buffer0.3119,6455,9850.109260672
NaOH (1M)0.3465,70922,0940.40334257
PBS0.1815,2551,9130.034923252
Polysorbate 801.83111.82558E-05
Total-5,477,726100

Consumable Costs

UCL-EEEEL.png

Consumable Costs Unit Cost ($) Annual Amount Annual Cost ($)
Dft DEF Cartridge1,0006363,000
Dft Membrane40010 m24,008
50 L Bag52101,050
Viral Exclusion Membrane13,35621280,476
Protein A6,000167 L1,000,337
SP-Sepharose High Performance1,20098 L117,915
HIC Butyl Sepharose High Performance2,0509 L18,332
Total--1,485,118

Equipment Cost $

Doxycline is added from a holding tank, absence of doxycline will make minimal difference to USP costs.

DSP costs are very high, that a cost reduction in the USP section has no significant difference to the total equipment costs

USP DSP Total Cost USP:DSP
732,0002,607,0003,339,0000.28
USP ' '
Equipment NameCost ($)
Stirred tank reactor539,000
Blending Tank193,000
DSP
Blending Tank191,000
Blending Tank159,000
Diafilter26,000
Chromatography Column148,000
Blending Tank137,000
Chromatography Column144,000
Dead-End Filter32,000
Blending Tank134,000
Diafilter22,000
Dead-End Filter32,000
Disposable Container-Skid0
Disk-Stack Centrifuge370,000Most expensive piece of equipment downstream
Dead-End Filter32,000
Chromatography Column192,000
Dead-End Filter32,000
Blending Tank134,000
Dead-End Filter32,000
Blending Tank127,000
Dead-End Filter32,000
Unlisted Equipment677,000
Total 3,385,000

Waste Treatment/Disposal Cost

Waste disposal costs are mainly for CEX and HIC

Waste Category Unit Cost ($/kg) Annual Amount (kg) Annual Cost ($) %
Solid Waste-000
Aqueous Liquid-156,6916,268100
IEX - Waste 0.0487,1903,48855.64
HIC- Waste0.0469,5002,78044.36
Organic Liquid-000
Emissions-88,58400
Total-245,2756,268100

Throughput Analysis

On SuperPro it assumes it would take 60 minutes to set up the Doxycline inlet This is 0.3 % of the overall process, delay in set up doesn't have a profound effect.


Process Data ' '
Annual Operating time7,104.66Hours
Annual Throughput132.36Kg/MP
Batch Throughput6.3Kg/MP
Plant Batch Time397.49Hours
Number of Batches per a year21Batches
Time Bottleneck EquipmentProduction FermenterPBR1
Throughput Utilization90%



























Retrieved from "http://2010.igem.org/Team:UCL_London/Doxycycline"