Refine
Year of publication
- 2024 (2)
- 2023 (14)
- 2022 (16)
- 2021 (11)
- 2020 (13)
- 2019 (17)
- 2018 (18)
- 2017 (12)
- 2016 (36)
- 2015 (30)
- 2014 (31)
- 2013 (29)
- 2012 (27)
- 2011 (28)
- 2010 (26)
- 2009 (24)
- 2008 (16)
- 2007 (20)
- 2006 (17)
- 2005 (20)
- 2004 (15)
- 2003 (14)
- 2002 (19)
- 2001 (18)
- 2000 (12)
- 1999 (16)
- 1998 (31)
- 1997 (25)
- 1996 (19)
- 1995 (36)
- 1994 (29)
- 1993 (21)
- 1992 (27)
- 1991 (15)
- 1990 (20)
- 1989 (20)
- 1988 (19)
- 1987 (16)
- 1986 (11)
- 1985 (7)
- 1984 (10)
- 1983 (10)
- 1982 (3)
- 1981 (3)
- 1980 (3)
- 1979 (8)
- 1978 (2)
- 1976 (2)
- 1975 (3)
- 1973 (2)
- 1972 (2)
- 1971 (2)
Document Type
- Article (597)
- Patent (117)
- Book (65)
- Conference Proceeding (34)
- Part of a Book (21)
- Report (5)
- Bachelor Thesis (3)
- Doctoral Thesis (3)
- Diploma Thesis (1)
- Preprint (1)
Language
- English (534)
- German (310)
- Multiple languages (2)
- Spanish (1)
Keywords
- Heparin (3)
- Bacillaceae (2)
- Biorefinery (2)
- Biotechnological application (2)
- Chemometrics (2)
- IR spectroscopy (2)
- NMR spectroscopy (2)
- Principal component analysis (2)
- Standardization (2)
- Subtilases (2)
- Subtilisin (2)
- bubble column (2)
- methanation (2)
- plug flow reactor (2)
- qNMR (2)
- (Poly)saccharides (1)
- (R)- or (S)- gamma-valerolactone (1)
- 4-hydroxy valeric acid (1)
- Algal Turf Scrubber (1)
- Algal–bacterial bioflm (1)
Institute
- Fachbereich Chemie und Biotechnologie (847) (remove)
In traditional microbial biobutanol production, the solvent must be recovered during fermentation process for a sufficient space-time yield. Thermal separation is not feasible due to the boiling point of n-butanol. As an integrated and selective solid-liquid separation alternative, solvent impregnated resins (SIRs) were applied. Two polymeric resins were evaluated and an extractant screening was conducted. Vacuum application with vapor collection in fixed-bed column as bioreactor bypass was successfully implemented as butanol desorption step. In course of further increasing process economics, fermentation with renewable lignocellulosic substrates was conducted using Clostridium acetobutylicum. Utilization of SIR was shown to be a potential strategy for solvent removal from fermentation broth, while application of a bypass column allows for product removal and recovery at once.
Heparin is a natural polysaccharide, which plays essential role in many biological processes. Alterations in building blocks can modify biological roles of commercial heparin products, due to significant changes in the conformation of the polymer chain. The variability structure of heparin leads to difficulty in quality control using different analytical methods, including infrared (IR) spectroscopy. In this paper molecular modelling of heparin disaccharide subunits was performed using quantum chemistry. The structural and spectral parameters of these disaccharides have been calculated using RHF/6-311G. In addition, over-sulphated chondroitin sulphate disaccharide was studied as one of the most widespread contaminants of heparin. Calculated IR spectra were analyzed with respect to specific structure parameters. IR spectroscopic fingerprint was found to be sensitive to substitution pattern of disaccharide subunits. Vibrational assignments of calculated spectra were correlated with experimental IR spectral bands of native heparin. Chemometrics was used to perform multivariate analysis of simulated spectral data.