Abstract
Experiments of ultrafiltration with diafiltration were performed on fermented broths of benzylpenicillin and clavulanic acid produced at pilot scale at CIPAN, SA to achieve solid/liquid separation, antibiotic recovery and soluble protein retention. This study was done using a laboratorial/pilot scale ultrafiltration facility from Paterson Candy International Ltd. whose modules have a tubular configuration. PVDF membranes with a molecular weight cut-off of 100 000 (FP10) and 200 000 (FP200) were assessed. Comparison between solvent extraction of benzylpenicillin and clavulanic acid from filtered broth and ultrafiltered broth was also done. It was concluded that ultrafiltration with diafiltration of fermented broths of antibiotics using the FP10 membrane is a valid alternative to the use of rotary vacuum filters, flocculants and filter aid, deserving a further study to establish the best operating conditions. An economic appraisal also seems to be of paramount importance.
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Abbreviations
- CF:
-
volumetric concentration factor
- C mg/1:
-
concentration
- ¯J 1/h m2 :
-
average permeate flux
- J(t) 1/h m2 :
-
permeate flux at time t
- Mass WB g:
-
mass of fermented broth
- P i :
-
bar inlet pressure of feed
- R BP %:
-
benzylpenicillin recovered by mass balance to the permeate, defined by equation (4)
- R CA%:
-
clavulanic acid recovered by mass balance to the permeate, defined by equation (4)
- ℜsolprot%:
-
retained soluble protein by mass balance to the permeate, defined by equation (5)
- SI%:
-
solvent increase
- SL%:
-
solvent losses
- T °C:
-
temperature
- t min:
-
time
- Δt :
-
min time difference
- Titre IU/g or IU/ml:
-
concentration of benzylpenicillin
- Titre μg/ml:
-
concentration of clavulanic acid
- V 1 or ml:
-
volume
- η%:
-
yield of antibiotic
- μ cp:
-
fluid viscosity
- BP:
-
benzylpenicillin
- CA:
-
clavulanic acid
- FP10:
-
100 000 MWCO ultrafiltration membrane
- FP200:
-
200 000 MWCO ultrafiltration membrane
- FB:
-
filtered broth
- IU:
-
international unit of activity
- ML:
-
mother liquors, i.e., extracted liquors
- MWCO:
-
molecular weight cut-off
- PCI:
-
Paterson Candy International Ltd.
- Prot FB:
-
protein in the filtered broth
- PVDF:
-
polyvinylidene fluoride
- RS:
-
rich solvent
- RFB:
-
rich filtered broth
- UF:
-
ultrafiltration
- 1 V diaf :
-
one diafiltration volume
- WB:
-
fermented broth (whole broth)
- C :
-
concentrate
- FB:
-
filtered broth
- Prot:
-
protein
- Prot FB:
-
protein in the filtered broth
- 0:
-
initial value
- P :
-
permeate
- Ext:
-
extraction
- Fil:
-
filtration
- UF:
-
ultrafiltration
- ML:
-
mother liquors, i.e., extracted liquors
- G :
-
global
- RS:
-
rich solvent
- WB:
-
fermented broth (whole broth)
References
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Code of Federal Regulations, CFR. 21§ 436.205
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To CIPAN-SA in which this work was done and where the fermented broths were produced. To JNICT/FSE for the funding of the project in the scope of which this work was done.
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Nabais, A.M.A., Cardoso, J.P. Ultrafiltration of fermented broths and solvent extraction of antibiotics. Bioprocess Engineering 13, 215–221 (1995). https://doi.org/10.1007/BF00367257
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DOI: https://doi.org/10.1007/BF00367257