Gluconate, predominantly produced by fermentation, is widely used in t
he form of sodium gluconate, gluconic acid or glucono-delta-lactone as
a bulk chemical. Because of undesirable by-products, the conventional
isolation and purification method (mainly ion exchange) is problemati
c, especially when gluconic acid is generated. In this paper the basic
behaviour of the recovery of gluconate using electrodialysis as well
as electrodialysis with bipolar membranes is described. Mass transfers
and conversion rates are measured depending on gluconate concentratio
n or current density. A typical flux was around 2.0 x 10(-4) kg/m(2)s.
In addition, current efficiencies, which influence specific energy co
nsumption, were considered. Around 3.0 x 10(6) J energy (excluding pum
ping) was necessary to isolate 1 kg gluconate. The achievable maximum
concentrations, which mainly depend on the ratio between mass transfer
of gluconate and water transport, were estimated at approximately 30%
(w/v) for the conventional and around 45% in case of the bipolar proc
ess.