umaric acid production by fermentation was operated in the United States during the 1940s, but later, this process was discontinued and replaced by chemical synthesis from petrochemical feedstocks, the latter being explained in a previous section. Nevertheless, the continuous increase of the petroleum prices has brought back the interest in fumaric acid production by submerged fermentation (Goldberg et al. 2006). Fumaric acid production by fermentation using Rhizopus species has been patented occasionally (Waksman 1943; Kane 1943; Lubowitz and La Roe 1958; La Roe 1959; Goldberg and Stieglitz 1986). In 1989, DuPont patented an improved fermentation process producing carboxylic acids (fumaric, succinic, malic, and mixtures thereof) by controlling dissolved oxygen levels between 30 and 80% (Ling and Ng 1989).
In the field of fumaric acid production by fermentation, there are many aspects determining the productivity of the fermentation process, such as the applied microbial strain and its morphology, the use of a neutralizing agent, and the applied feedstock. Those aspects are reviewed and analyzed in more detail in the following sections.