“…The previous methods for the production of lactic acid, salts of lactic acid, or SCP (single cell protein), by fermentation of cheese whey, suffered from one or more of the following disadvantages: (i) there was a long lag period prior to active lactic acid fermentation and/or unus-770 REDDY, HENDERSON, AND ERDMAN ually long fermentation times that required greater fermentor capacity and increased operational costs (4, 36; Czarnetzky, U.S. Patent 2,094,437,1959); (ii) manual procedures used for the addition of ammonia or calcium ion to neutralize the lactic acid produced during the fermentation were tedious and contributed to increased product variability (18,36; Czarnetzky, U.S. Patent 2,094,437, 1959; Jansen, Dutch Patent 57848, 1948; Perquin, Dutch Patent 58545, 1946); (iii) large levels of inocula (10 to 20% by volume) were required to obtain vigorous fermentation and, hence, were less economical (2,4,6,36,43; Czarnetzky, U.S. Patent 2,094,437, 1959; Jansen, Dutch Patent 57848, 1945); (iv) putrefactive spoilage of the fermentations was encountered (2); (v) the crude protein content of the product was relatively low (4,6; Czarnetzky, U.S. Patent 2,094,437, 1959; Perquin, Dutch Patent 58545, 1946); (vi) relatively high costs were involved in the pastuerization or sterilization of whey prior to fermentations (2, 6, 36; Czarnetzky, U.S. Patent 2,094,437, 1959); (vii) there were high aeration costs during fermentation (4, 6, 32); and (viii) there were palatability problems for the animals with the product that resulted in decreased dry matter intake (21).…”