Fish industry by-products can account for up to 75% of the catch depending on postharvest or industrial preparation processes. Different terms such as 'fish waste', 'by-product' and 'rest raw materials' have been used. The review gives an overview of value-added processes that provide an alternative to low-profit uses such as silage, fish meal and mince. The preparation of different by-product fractions such as fish blood, marine lipids, omega-3 fatty acids, fish protein fractions and bioactive components with nutraceutical potential, i.e. antioxidants and bioactive peptides, is considered. There are several future opportunities for the preparation of high-value by-products such as enzymes, minerals and other bioactive substances including hydroxyapatite, phosphorus, taurine and creatine. Both regulatory status and future market potential need to be considered. In addition, there is a need for technologies that maintain good quality by-products and 'simple' processes to produce bulk products for further refining.
The effects of process conditions and growth kinetics on the production of the bacteriocin sakacin P by Lactobacillus sakei CCUG 42687 have been studied in pH-controlled fermentations. The fermentations could be divided into phases based on the growth kinetics, phase one being a short period of exponential growth, and three subsequent ones being phases of with decreasing specific growth rate. Sakacin P production was maximal at 20 degrees C. At higher temperatures (25-30 degrees C) the production ceased at lower cell masses, when less glucose was consumed, resulting in much lower sakacin P concentrations. With similar media and pH, the maximum sakacin P concentration at 20 degrees C was seven times higher than that at 30 degrees C. The growth rate increased with increasing concentrations of yeast extract, and the maximum concentration and specific production rate of sakacin P increased concomitantly. Increasing tryptone concentrations also had a positive influence upon sakacin P production, though the effect was significantly lower than that of yeast extract. The maximum sakacin P concentration obtained in this study was 20.5 mg l(-1). On the basis of the growth and production kinetics, possible metabolic regulation of bacteriocin synthesis is discussed, e.g. the effects of availability of essential amino acids, other nutrients, and energy.
The rate of diffusion of serum albumin (MW 6.9 x 10(4) D) out of beads of calcium alginate gels depends upon the concentration and uronic acid composition of the alginate (ManA/GulA ratio), the conditions under which the beads are produced, the pH, and the temperature. The diffusion coefficient decreases with increasing alginate concentration, and (ManA/GulA) ratio and with decreasing pH. Diffusion out of the beads, in which the alginate is uniformly distributed (homogeneous gel), is faster than out of the beads in which the alginate is concentrated at the surface (inhomogeneous gel). The temperature dependence of the diffusion coefficient follows the Arrhenius law, with an activation energy of approximately 23 kJ x mol(-1).
This work investigated iron-catalyzed lipid oxidation in marine phospholipid liposomes. Oxygen consumption was used as a method to study lipid oxidation at pH 5.5 and 30 degrees C. The relationship between consumed oxygen and amount of peroxides (PV) and thiobarbituric reactive substances (TBARS) formed showed that both Fe2+ and Fe3+ catalyzed lipid oxidation. When Fe2+ was added to liposomes at a concentration of approximately 10 microM, an initial drop in dissolved oxygen (oxygen uptake rate >258 microM/min), followed by a slower linear oxygen uptake (oxygen uptake rate 4-6 microM/min), was observed. Addition of Fe3+ induced only the linear oxygen uptake. The initial fast drop in dissolved oxygen was due to oxidation of Fe2+ to Fe3+ by preexisting lipid peroxides (rate 79 microM Fe2+/min). Fe3+ is reduced by peroxides to Fe2+ at a slow rate (0.25 microM Fe3+/min at 30 degrees C) in a pseudo-first-order reaction. The redox cycling between Fe2+ and Fe3+ leads to an equilibrium between Fe2+ and Fe3+ resulting in a linear oxygen uptake. During the linear oxygen uptake, the interaction of Fe (3+) with lipid peroxide is the rate-limiting factor. Both alkoxy and peroxy radicals are formed by breakdown of peroxides by Fe2+ and Fe3+. These radicals react with fatty acids giving lipid radicals reacting with oxygen.
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