Method for high efficiency reverse osmosis operation

摘要

A process for treatment of water. Hardness and non-hydroxide alkalinity are removed from feedwaters in amounts to substantially avoid scaling when concentrated. Sparingly ionizable components in the feedwater are urged toward increased ionization by increasing the pH of the feedwater, and, in an embodiment, up to about pH 10.5, or higher. In this manner, species such as silica become highly ionized, and (a) their rejection by membranes used in the process is significantly increased, and (b) their solubility in the reject stream from the membrane process is significantly increased. Sparingly ionized species such as boron, silica, and TOC are highly rejected, and thus, their passage through the membrane is reduced by a factor of ten or more. Recovery ratios of ninety percent (90%) or higher are achievable with many feedwaters, while simultaneously achieving a substantial reduction in cleaning frequency of membranes used in the process.

主权项

1. A process for treatment of a feedwater stream with reverse osmosis membrane separation equipment, to produce a low solute containing product stream and a high solute containing reject stream, said process comprising:
(a) providing a feedwater stream containing solutes therein, said solutes comprising (i) hardness, (ii) alkalinity, and (iii) at least one molecular species which is sparingly ionized when in neutral or near neutral pH aqueous solution, said at least one molecular species comprising one or more of (1) at least some TOC, or (2) at least some silica, or (3) at least some boron; (b) effectively eliminating the tendency of said feedwater to form scale when said feedwater is concentrated at a selected pH, by treating the feedwater stream in a hydrogen form cation exchange resin to (i) remove substantially all hardness from said feedwater stream, (ii) remove substantially all alkalinity from said feedwater stream, and (iii) remove dissolved carbon dioxide created during removal of said hardness and of said alkalinity; (c) raising the pH of the product from step (b) to a selected pH of ten (10) or more, by adding a selected alkali thereto, to urge said at least one molecular species which is sparingly ionized when in neutral or near neutral pH aqueous solution toward increased ionization; (d) passing the product from step (c) above through continuously operated reverse osmosis membrane separation equipment, to concentrate said feedwater at a recovery rate of ninety percent (90%) or more; (e) maintaining a stable normalized production rate of said product stream; and (f) maintaining a stable silica rejection rate in said reverse osmosis membrane separation equipment.