Water purification process

Claim 2

In the process of purification of polluted water comprising percolating the water to be treated downward through a submerged fixed bed of granular material with insufflation, at an intermediate level of the bed, of a rising oxygenated gas current, the improvement wherein the linear velocity of the water through the bed exceeds 2 m/hr and the delivery of water to be treated and the delivery of oxygenated gas are otherwise regulated such that the following relations are satisfied: ##EQU10## wherein Q 1 is the delivery of oxygenated gas in m 3 /hr, Q 2 is the delivery of water to be treated in m 3 /hr, ε is the porosity of the granular material bed, ε being 0.45 and 0.55, α is the maximum fraction of the volume that can be occupied by the gas without affecting the effectiveness of the treatment, α being 0.2 to 0.6, S is the bed section in m 2 , h is the height of the bed in meters, v is the vertical component of the average speed of the ascending gas bubbles in m/hr, v being 200 to 400 m/hr, K 1 is a constant corresponding to the fraction of volume of bed occupied by immobilized gas pockets in m 3 , K 1 being 0.02 to 0.08 m 3 , K 2 is the concentration of gas in oxygen in kg/m 3 , K 2 being 0.2 to 1.40 kg/m 3 , K 3 is the value of the demand for oxygen that 1 m 3 of granular material can satisfy in 1 hour under operating conditions of the process in kg O 2 /m 3 of granular material/hr, K 3 being less than 0.8 kg/m 3 /hr, R is the total transfer yield (or the fraction: weight of oxygen effectively dissolved/weight of oxygen injected in the bed), R being a function of the saturation solution (C S ) and real concentration (C) of oxygen in the bed according to the relation R=K(C.sub.S -C) wherein K is between 2.7×10 -3 and 25×10 -3 (mg/l) -1 m -1 , and OD is the demand for oxygen to be met, in kg per unit of volume of water to be treated, OD being between 0.7 and 1.2 times BOD 5 or total OD is 0.7 to 1.2 times BOD 5 plus 4 to 5 times N (of NH 4 ); and wherein said granular material includes a material exhibiting a sufficient mechanical resistance so as not to sustain abrasion during bed washing, a granulometry between about 1 and about 8 mm, and an aptitude for fixing at least one of the elements necessary for biochemical reactions.

Claim 3

In a process of purification of polluted water comprising percolating the water to be treated downward through a submerged fixed bed of granular material with insufflation, at an intermediate level of the bed, of a rising oxygenated gas current, the improvement wherein the water remains in contact with the mass of granular material above said intermediate level for a time of contact less than 30 minutes and the delivery of water to be treated and the delivery of oxygenated gas are otherwise regulated such that the following relations are satisfied: ##EQU11## wherein Q 1 is the delivery of oxygenated gas in m 3 /hr, Q 2 is the delivery of water to be treated in m 3 /hr, ε is the porosity of the granular material bed, ε being 0.45 and 0.55, α is the maximum fraction of the volume that can be occupied by the gas without affecting the effectiveness of the treatment, α being 0.2 to 0.6, S is the bed section in m 2 , h is the height of the bed in meters, v is the vertical component of the average speed of the ascending gas bubbles in m/hr, v being 200 to 400 m/hr, K 1 is a constant corresponding to the fraction of volume of bed occupied by immobilized gas pockets in m 3 , K 1 being 0.02 to 0.08 m 3 , K 2 is the concentration of gas in oxygen in kg/m 3 , K 2 being 0.2 to 1.40 kg/m 3 , K 3 is the value of the demand for oxygen that 1 m 3 of granular material can satisfy in 1 hour under operating conditions of the process in kg O 2 /m 3 of granular material/hr, K 3 being less than 0.8 kg/m 3 /hr, R is the total transfer yield (or the fraction: weight of oxygen effectively dissolved/weight of oxygen injected in the bed), R being a function of the saturation solution (C S ) and real concentration (C) of oxygen in the bed according to the relation R=K(C.sub.S -C) wherein K is between 2.7×10 -3 and 25×10 -3 (mg/l) -1 m -1 , and OD is the demand for oxygen to be met, in kg per unit of volume of water to be treated, OD being between 0.7 and 1.2 times BOD 5 or total OD is 0.7 to 1.2 times BOD 5 plus 4 to 5 times N (of NH 4 ); and wherein said granular material includes a material exhibiting a sufficient mechanical resistance so as not to sustain abrasion during bed washing, a granulometry between about 1 and about 8 mm, and an aptitude for fixing at least one of the elements necessary for biochemical reactions.

Claim 4

In a process of purification of polluted water comprising percolating the water to be treated downward through a submerged fixed bed of granular material with insufflation, at an intermediate level of the bed, of a rising oxygenated gas current, the improvement wherein the water remains in contact with the mass of granular material above said intermediate level for a time of contact less than 30 minutes and the delivery of water to be treated and the delivery of oxygenated gas are otherwise regulated such that the following relations are satisfied: ##EQU11## wherein Q 1 is the delivery of oxygenated gas in m 3 /hr, Q 2 is the delivery of water to be treated in m 3 /hr, ε is the porosity of the granular material bed, ε being 0.45 and 0.55, α is the maximum fraction of the volume that can be occupied by the gas without affecting the effectiveness of the treatment, α being 0.2 to 0.6, S is the bed section in m 2 , h is the height of the bed in meters, v is the vertical component of the average speed of the ascending gas bubbles in m/hr, v being 200 to 400 m/hr, K 1 is a constant corresponding to the fraction of volume of bed occupied by immobilized gas pockets in m 3 , K 1 being 0.02 to 0.08 m 3 , K 2 is the concentration of gas in oxygen in kg/m 3 , K 2 being 0.2 to 1.40 kg/m 3 , K 3 is the value of the demand for oxygen that 1 m 3 of granular material can satisfy in 1 hour under operating conditions of the process in kg O 2 /m 3 of granular material/hr, K 3 being less than 0.8 kg/m 3 /hr, R is the total transfer yield (or the fraction: weight of oxygen effectively dissolved/weight of oxygen injected in the bed), R being a function of the saturation solution (C S ) and real concentration (C) of oxygen in the bed according to the relation R=K(C.sub.S -C) wherein K is between 2.7×10 -3 and 25×10 -3 (mg/l) -1 m -1 , and OD is the demand for oxygen to be met, in kg per unit of volume of water to be treated, OD being between 0.7 and 1.2 times BOD 5 or total OD is 0.7 to 1.2 times BOD 5 plus 4 to 5 times N (of NH 4 ); and wherein said granular material includes a material exhibiting a sufficient mechanical resistance so as not to sustain abrasion during bed washing, a granulometry between about 1 and about 8 mm, and an aptitude for fixing at least one of the elements necessary for biochemical reactions.

Claim 5

A process in accordance with claims 1 or 2 wherein the granular material is activated carbon and the injection of oxygenated gas is in the lower zone of the activated carbon bed.

Claim 6

A process in accordance with claims 1 or 2 wherein said oxygenated gas is selected from the group consisting of air, pure oxygen, and an ozonized gaseous mixture coming from recycling of an atmosphere rich in ozone lying over water previously disinfected with ozone.

Claim 7

A process in accordance with claim 4, further including the step of controlling and regulating the supply of oxygenated gas serving for injection into the bed by means of a probe for measuring dissolved oxygen, said probe being placed in the water to be treated.

Claim 8

A process in accordance with claims 1 or 2 further including the step of ozonizing the water to be purified prior to said percolating step.

Claim 9

A process in accordance with claims 1 or 2 wherein said polluted water comprises surface or layer waters to be made potable, sewage water or industrial water.

Claim 10

A process in accordance with claims 1 or 2, wherein said granular material comprises a double bed containing grains of activated carbon in the upper part, and, in the lower part, grains of a finer and denser material of sand or the like.

Claim 11

A process in accordance with claim 8, wherein said granular material further includes a layer of material of intermediate density between said activated carbon and said sand-like material.

Claim 12

A process in accordance with claim 9 wherein said material of intermediate density is anthracite.

Claim 13

A process in accordance with claims 1 or 2, wherein said granular material comprises at least an upper portion, in the volume above the point of insufflation, of a member of the group consisting of fixed clays (chamottes), chamottes doped with trace elements, raw clays, hydrated silicates and activated aluminas.

Claim 14

A process in accordance with claim 11 wherein said granular material further includes, below said upper portion, a lower portion of finer and denser material of sand or the like.

Claim 15

A process in accordance with claim 12, wherein said granular material further includes a layer of intermediate density between said upper and lower portions.

Claim 16

A process in accordance with claim 13, wherein said material of intermediate density is anthracite.