초록 ▼

A process has steps of one or more of aerobic treatment to remove COD and nitrify a waste stream, anoxic treatment to denitrify a waste stream, anoxic treatment to remove selenium and anaerobic treatment to remove heavy metals and sulphur. The process may be used to treat, for example, FGD blow down

A process has steps of one or more of aerobic treatment to remove COD and nitrify a waste stream, anoxic treatment to denitrify a waste stream, anoxic treatment to remove selenium and anaerobic treatment to remove heavy metals and sulphur. The process may be used to treat, for example, FGD blow down water. The process may further include one or more of (a) membrane separation of the waste stream upstream of the anoxic digestion to remove selenium, (b) dilution upstream of the biological treatment step, (c) physical/chemical pretreatment upstream of the biological processes or dilution step to remove TSS and soften the waste stream, or (d) ammonia stripping upstream of the biological treatment steps or dilutions step. These processes may be provided in a variety of suspended growth or fixed film reactors, for example a membrane bioreactor or a fixed film reactor having a GAC bed. Processes for biological treatment of inorganic compounds in a fixed medium reactor is described including steps of one or more of maintaining desired ORP levels, optionally by controlling nutrient addition, and removing solids or gas bubbles from the medium bed.

대표청구항 ▼

1. A process for treating water comprising flue gas desulphurization blowdown water to remove selenium from the water comprising the steps of, a) treating the water to reduce its total suspended solids concentration;b) flowing the water through a first media bed reactor and then through a second med

1. A process for treating water comprising flue gas desulphurization blowdown water to remove selenium from the water comprising the steps of, a) treating the water to reduce its total suspended solids concentration;b) flowing the water through a first media bed reactor and then through a second media bed reactor;c) adding one or more nutrients to the water flowing through the first media bed reactor in an amount such that the oxygen reduction potential of the water at an outlet of the first media bed reactor is between −50 mV and −200 mV; and,d) adding one or more nutrients, in addition to the one or more nutrients of step c), to the water flowing through the second media bed reactor such that the oxygen reduction potential of the water at an outlet of the second media bed reactor is between −150 mV and −350 mV. 2. The process of claim 1 comprising a step of periodically bumping one or more of the first media bed reactor and the second media bed reactor at least one per week to release solids. 3. The process of claim 1 wherein the one or more nutrients comprise molasses. 4. The process of claim 1 wherein the one or more nutrients added in step c) comprise dibasic acid (DBA) that was added to the water to during a flue gas desulphurization process.