Investigation of production of dextran and dextransucrase by Leuconostoc mesenteroides immobilized within porous stainless steel.

Cells of Leuconostoc mesenteroides were immobilized within porus, stainless-steel (SS) supports and used for dextransucrase (DS) and dextran production. The pore size of the support significantly affected the dextran yields, which were greatest with average pore sizes of 2-5 microm. All immobilized-cell biocatalysts in porous stainless steel produced higher yields than free cells, with the exception of cells confined in submicrometer pores (0.5 microm). Coating supports of larger pore size (40 and 100 microm) with calcium alginate enhanced the cell-loading capacity of the supports and increased dextran and fructose yields in the cell-free broth. Controlled, fed-batch, DS production (activation), as a step preliminary to dextran production, significantly improved the subsequent dextran and fructose yields and shortened the time required to attain the maximum such yields. Scanning electron microscopy (SEM) of immobilized L. mesenteroides in stainless steel shows an irregular pattern of the microorganism inside the pores of the solid supports. Coating the porous solid supports with a cell-free calcium alginate layer led to an increase in the cell density inside the support. Cell growth inside the coated, porous stainless steel had no distinct growth form.

Production of dextransucrase by Leuconostoc mesenteroides immobilized in calcium-alginate beads: I. Batch and fed-batch fermentations.

In batch fermentation Leuconostoc mesenteroides immobilized in calcium alginate beads produced a total dextransucrase activity equal to about 93% of that by free, suspended bacterial cells under comparable conditions in a bubble column reactor. Continuous sucrose feeding (5 g/L h) to the immobilized-cell culture in the airlift bioreactor increased production of enzymatic activity by about 107% compared with ordinary batch operation of this reactor. About 14% of the enzymatic activity produced by the immobilized cells appears as soluble activity in the cell-free broth compared with about 40% in case of free cells. In an airlift bioreactor, both the soluble and the intact (sorbed and entrapped) enzymatic activity produced by the immobilized bacterial cells was about 34% greater under automatic pH control, compared to that produced in a bubble column reactor with only manual pH control. During formation of dextran by intact enzyme within cells and beads, declines are observed in apparent enzymatic activity.

Production of dextransucrase and dextran by Leuconostoc mesenteroides immobilized in calcium-alginate beads: II. Semicontinuous fed-batch fermentations.

Cells of Leuconostoc mesenteroides immobilized in calcium alginate beads were used to produce dextransucrase (DS) in three sequential cycles of semicontinuous fed-batch fermentations. Each cycle consisted of a fed-batch DS production period of 24 h followed by a batch dextran production period for another 24 h. Free, suspended cells were used in only one cycle of fed-batch DS production followed by a dextran production period. It was impractically tedious to separate and reuse free cells. Increasing sucrose feed rate from 5 to 10 g/L h led to increases of the total enzymatic activity by about 88% with immobilized cells and by about 100% with free cells. In DS fed-batch semicontinuous fermentation, total enzymatic activity produced by immobilized cells was 1.35 and 1.56 times greater than that produced by free cells with respective sucrose feeding rates of 10 and 5 g/L h. These increases in enzyme productivity with immobilized cells, however, required total overall operating times three times longer (three cycles) than with free cells (one cycle). Growing the microorganism at optimum conditions for DS production also increased the dextran yield and shortened the time of conversion of sucrose to dextran, regardless of whether the cells were free or immobilized. Moreover, during three cycles of semicontinuous operation (144 h) immobilized cells produced more than three times as much dextran as free cells during one cycle (24 h).

Effect of beta-cyclodextrin on production of L-phenylacetyl carbinol by immobilized cells of Saccharomyces cerevisiae.

The rate and extent of microbial transformation of higher concentrations of benzaldehyde substrate to L-phenylacetyl carbinol (L-PAC) by immobilized cells of Saccharomyces cerevisiae ATCC 834 was markedly stimulated by addition of different concentrations of beta-cyclodextrin (BCD) to the fermentation medium. With 0.5, 1.0, and 1.5% BCD in the fermentation medium and cumulative doses of benzaldehyde of 12 and 14 g/L, significantly higher yields of L-PAC were obtained, about one- to twofold that of the yields of the control experiments. The favorable effects of BCD were evident in spite of its presence in stoichiometric concentrations significantly lower than those of benzaldehyde. The presence of BCD also appeared to stimulate microbial growth slightly. Enhanced cellular activity was reflected by faster D-glucose consumption and faster benzaldehyde utilization in the presence of BCD.

Production of L-phenylacetyl carbinol by immobilized yeast cells: I. Batch fermentation.

Immobilization of Saccharomyces cerevisiae ATCC 834 within alginate beads enhances microbiological conversion of benzaldehyde to L-phenylacetyl carbinol (L-PAC), a precursor employed for synthesis of L-ephedrine. Yields of 90% L-PAC on benzaldehyde (initially 0.6% in medium) were obtained with immobilized cells, in contrast to about 10% with free cells which tend to form pellets in the presence of benzaldehyde. The predominant favorable action of immobilization appears to be a reduction in the toxic or inhibitory effects of benzaldehyde. With an initial benzaldehyde concentration of about 0.6% in the medium the optimum cell mass concentration was observed to be about 28 g cell mass (immobilized) per liter of medium.

Production of L-phenylacetyl carbinol by immobilized yeast cells: II. Semicontinuous fermentation.

The cyclic, semicontinuous production of L-phenylacetyl carbinol (L-PAC) from a benzaldehyde substrate by Saccharomyces cerevisiae ATCC 834 immobilized in calcium alginate beads was substantially enhanced to about 4.5 g/L in a second cycle by reactivation in fresh medium for 24 h, following an earlier 24-h period of production from substrate. Intermittent feeding of benzaldehyde was employed (four doses in 3 h). In subsequent similar cycles, however, the production returned to that produced in the first cycle, viz. L-PAC concentration of 2-3 g/L in the medium. Production of L-PAC was also increased by adaptation of the cells over 200 h of exposure to the benzaldehyde substrate (compared to wild-type cells) and by continuous (as compared to intermittent) feeding of the substrate. A liter as great as 10 g/L was obtained with wild-type cells by continuous feeding of benzaldehyde over 6 h. Immobilization not only protected the cells from toxic effects of substrate but also permitted them to be used during 7 cycles of semicontinuous operation over more than 200 h.

Comparative study of production of dextransucrase and dextran by cells of Leuconostoc mesenteroides immobilized on Celite and in calcium alginate beads.

In fed-batch fermentation, cells of L. mesenteroides immobilized on three types of Celite were used to produce dextransucrase (DS) followed by production of dextran. A layer of calcium alginate on the porous Celite R630 particles improved their mechanical stability, increased the amount of soluble DS produced and decreased the cell leakage from the highly porous support. Enzyme production with the immobilized cell cultures was significantly affected by both pore and particle size. Immobilized cultures using Celite R648 (average particle radius of 200 microm and pore size of 0.14 microm) produced the highest total enzymatic activity, followed by Celite R633, alginate-coated Celite R630, Celite R630, and then calcium alginate beads. Culture of free cells produced about 18% more total enzymatic activity than immobilized cells in calcium alginate beads, but about 64% less than immobilized cells on Celite R630. It is expected that larger amounts of enzymatic activity than measured are immobilized inside the alginate-coated Celite R630 and calcium alginate beads due to the mass transfer limitation conferred by the dextran product formed therein. The dextran yield from conversion of sucrose to dextran and fructose with all such enzyme-enriched, immobilized-cell cultures was higher than that obtained from free-cell culture under similar conditions.