Abstract A system is provided to treat wastewater from a metal-working facility, such as an automotive manufacturing plant in a bioreactor using live microorganisms. Such wastewater contains waste fluids which are a mixture of relatively easily biodegradable fats and oils, much less easily biodegradable synthetic fluids, oils and greases, and nonbiodegradable material including inorganic finely divided solids such as metal and silicon carbide particles. Such waste fluids require a hydraulic retention time (HRT) and a solids retention time (SRT) which is 10 times greater than for sewage. High quality water is separated from suspended solids which are removed from the reactor at an essentially constant rate and fed to an ultrafiltration membrane. Concentrate is recycled to the reactor, except for a bleed stream to remove solids periodically. The membranes acquire a long and effective life despite large variations in membrane flux, because of a permeate recycle which permits operation of the bioreactor at constant volume; permits flow of feed wastewater to the reactor at constant flow rate; and allows operation of the membrane modules at a relatively low pressure in a narrow range which does not damage the membranes. Such operation of the bioreactor allows one to use a reactor which is one-half the size (volume) than one which would be required with a system without a permeate recycle. Effective and long-lived operation of the membranes is obtained by filtering out (through a 140 mesh screen) all solids greater in diameter than about 106 μm. Pilot plant tests conducted with wastewater from automobile manufacturing plants over a period of more than a year provide evidence of the surprising effectiveness of the system over a prolonged period.
A wastewater treatment system operatively connected between a source of wastewater containing waste fluids from a metal-working plant and an outlet for treated effluent, comprising, (a) a vessel large enough to hold said wastewater delivered at a variable rate of flow and to equalize the rates of flow to a predetermined essentially constant rate removed from said vessel; (b) means to remove free oil from said wastewater to provide a skimmed wastewater; (c) filtration means having a mesh size small enough to remove finely divided solids larger than 106 μm which are injurious to membrane means and provide a solids-depleted feed; (d) a bioreactor means in which is confined an essentially constant volume of a reaction mass with means for aerating skimmed and solids-depleted feed, and for contacting said feed with waste-degrading microorganisms mixed therein; (e) pump means for withdrawing a suspension of biomass from said bioreactor at an essentially constant rate of flow, and impelling said suspension at elevated pressure in the range from 170 kPa to 1035 kPa (25-150 psig); (f) membrane filtration means in direct, open flow-receiving communication with said pump means, said membrane filtration means having a pore size in the range from 0.01 μm to 0.1 μm, including plural membrane elements adapted to separate said suspended solids in a concentrate stream, from water permeate which is essentially free of solids, and means to duct said permeate away from said system; (g) means to return said concentrate stream to said bioreactor means; and, (h) means to return a minor portion of said permeate to said bioreactor means.
Claim 2
Dependent Claim
261 words
A wastewater treatment system operatively connected between a source of wastewater containing waste fluids from a metal-working plant and an outlet for treated effluent, comprising, (a) a vessel large enough to hold said wastewater delivered at a variable rate of flow and to equalize the rates of flow to a predetermined essentially constant rate removed from said vessel; (b) means to remove free oil from said wastewater to provide a skimmed wastewater; (c) filtration means having a mesh size small enough to remove finely divided solids larger than 106 μm which are injurious to membrane means and provide a solids-depleted feed; (d) a bioreactor means in which is confined an essentially constant volume of a reaction mass with means for aerating skimmed and solids-depleted feed, and for contacting said feed with waste-degrading microorganisms mixed therein; (e) pump means for withdrawing a suspension of biomass from said bioreactor at an essentially constant rate of flow, and impelling said suspension at elevated pressure in the range from 170 kPa to 1035 kPa (25-150 psig); (f) membrane filtration means in direct, open flow-receiving communication with said pump means, said membrane filtration means having a pore size in the range from 0.01 μm to 0.1 μm, including plural membrane elements adapted to separate said suspended solids in a concentrate stream, from water permeate which is essentially free of solids, and means to duct said permeate away from said system; (g) means to return said concentrate stream to said bioreactor means; and, (h) means to return a minor portion of said permeate to said bioreactor means.
Claim 3
Dependent Claim
44 words
The wastewater treatment system of claim 1 wherein said membrane filtration means includes a preliminary filtration membrane having a pore size smaller than 0.5 μm upstream of said membrane filtration means having a pore size in the range from 0.01 μm to 0.1 μm.
Claim 4
Dependent Claim
49 words
The wastewater treatment system of claim 1 wherein said membrane filtration means includes a subsequent filtration membrane having a pore size in the range from 0.001 μm to 0.01 μm downstream of said membrane filtration means having a pore size in the range from 0.01 μm to 0.1 μm.