Paracoccus denitrificans for the effluent recycling during continuous denitrification of liquid food.

Nitrate is an undesirable component of several foods. A typical case of contamination with high nitrate contents is whey concentrate, containing nitrate in concentrations up to 25 l. The microbiological removal of nitrate by Paracoccus denitrificans under formation of harmless nitrogen in combination with a cell retention reactor is described here. Focus lies on the resource-conserving design of a microbal denitrification process. Two methods are compared. The application of polyvinyl alcohol-immobilized cells, which can be applied several times in whey feed, is compared with the implementation of a two step denitrification system. First, the whey concentrate's nitrate is removed by ion exchange and subsequently the eluent regenerated by microorganisms under their retention by crossflow filtration. Nitrite and nitrate concentrations were determined by reflectometric color measurement with a commercially available Reflectoquant device. Correction factors for these media had to be determined. During the pilot development, bioreactors from 4 to 250 mg x L(-1) and crossflow units with membrane areas from 0.02 to 0.80 m(2) were examined. Based on the results of the pilot plants, a scaling for the exemplary process of denitrifying 1,000 tons per day is discussed.

Isolation of bovine lactoferrin, lactoperoxidase and enzymatically prepared lactoferricin from proteolytic digestion of bovine lactoferrin using adsorptive membrane chromatography.

A new downstream procedure for the isolation of bovine lactoferrin (bLf), lactoperoxidase and bovine lactoferricin (LfcinB) from sweet cheese whey was developed at the laboratory scale, based on membrane adsorber technology. The procedure was upscaled later on to an industrially relevant scale for the purificationof sweet whey concentrate with a recovery yield for lactoferrin of more than 90%. Based on these results the industrial process for 1 x 10(8) kg whey per year was projected. These high-value proteins were downstreamed by using cation-exchange membrane systems (Sartobind S, Sartorius, Göttingen, Germany). These strongly acidic membranes trap proteins in its anionic form. The dynamic loading capacity for both proteins as well as the optimal elution profiles with sodium chloride gradients were derived from laboratory experiments using membrane modules with 15-75 cm2 membrane material. Further investigations were performed with 1 m2 modules in a continuous process mode. The enzymatic preparation of LfcinB from bLf was performed by pepsin hydrolysis and the isolation of LfcinB was directly carried out from the enzymatic digest mixture. The identification of the proteins was performed with matrix-assisted laser desorption ionisation mass spectrometry (MALDI-MS). LfcinB and bLf were both tested afterwards in biological assays in order to show not only the efficiency of the downstreaming process in regard to product quantity but also to product quality (biological activity).