A process for treatment of water via membrane separation equipment. A
feedwater is maintained or adjusted to a pH of 4.3 or lower, and fed to a
membrane separation system. In this manner, species such as TOC become
more ionized, and (a) their rejection by the membrane separation process
is significantly increased, and (b) their solubility in the reject stream
from the membrane process is significantly increased. Passage TOC through
the membrane is significantly reduced. A recovery ratio of eighty percent
(80%) or higher is achievable with most feedwaters, while simultaneously
achieving a substantial reduction in cleaning frequency of the membrane
separation equipment. The method is particularly useful for the
preparation of high purity water.