An improved method for operating a down-flow granular medium filter is disclosed which increases the effective filtration time between backwashes. The filter tank cell is divided into a plurality of subcells, each individually adapted and controlled for periodic intermittent upwardly-directed pulses of fluid passed through the filter bed within each subcell from an array of orifices beneath or in the bed. During the filtration run, one subcell is pulsed to improve the porosity of that portion of the filter bed while the remainder of the subcells continue to filter wastewater. After initiation of the first pulsing cycle for a subcell, additional subcell pulsing cycles are initiated sequentially. At the end of the filtration run the whole filter cell is backwashed to remove particulate matter from the bed and prepare the bed for the next filtration run.
A biological oxidation filter system can be used as a pretreatment process in water treatment, or for processing sewage or wastewater by reproducing the purification mechanisms in nature environments. It has a physical screening function and an oxidation function through the aeration and biological decomposition. The biological oxidation filter system includes: a raw water inflow unit; a biological contact filter unit; a filtrate outflow unit; an oxidation air supply unit supplying air and/or oxygen in order to provide a proper growth environment for microbial flora and perform the oxidation in the biological contact filter unit; and an air backwashing unit and a water back washing unit for backwashing the filter media when the biological contact filter unit is blocked. As the pretreatment process, the biological oxidation filter system efficiently removes particulate matters, organic substances, ammonia nitrogen, ferrous, manganese, odor and algae, thereby improving contaminated raw water quality to get better final treatment effects. As the wastewater treatment process, the biological oxidation filter system removes the turbid matters, ammonia nitrogen and odor, and thus can also be employed as a high quality wastewater purification system to keep streams and lakes from contamination.
A process for the treatment of water using a granular bed (3) of granular support materials of a volumic mass less than that of the water to be treated. According to this process, each washing cycle comprises interrupting the withdrawal of treated water and stopping the feed of water to be treated in such a manner that the granular bed (3) floats in a given volume VL of water, admitting cleansing air into the reactor for assuring agitation of the floating bed, interrupting the admission of air in order to permit a separation of the granular materials and sediment by their difference in volumic mass, with decantation of said sediment and flotation of said materials, and evacuating the sediments at the base of the reactor as well as the water contained therein for evacuating the granular bed (3).
Storm water runoff is treated by passing the runoff through a bed of high quality leaf compost material to remove pollutants from the runoff prior to discharge into a water receiving system, such as a river, lake or storm water drainage system. Apparatus for treating storm water runoff is disclosed having at least one chamber for containing compost defined by a pair of opposed side walls and a pair of opposed end walls; an influent pathway for providing storm water to the compost chamber, a drain field positioned beneath the compost chamber for receiving storm water from the compost chamber, a layer of water permeable material interposed between the compost chamber and the drain field providing fluid communication between the compost chamber and the drain field while preventing the flow of compost material into the drain field, and a storm water outlet in fluid communication with the drain field for discharging treated storm water from the apparatus.
Improved methods are disclosed for cleansing a plurality of seriate filter beds in automatic backwash filtering systems by backwashing the beds one at a time with backwash liquid from an effluent channel common to seriate effluent ports of the plurality of filter beds and pumping the backwash liquid seriatim through separate effluent ports of individual filter beds and then flowing filtered effluent from each bed through its effluent port into the effluent channel, repeating such steps of backwashing and flowing filtered effluent on individual filter beds until all the filter beds in the system have been backwashed wherein, simultaneously with the backwashing of a second bed, waste liquid from the first bed is pumped through its port while the waste liquid is monitored for turbidity and such waste liquid pumping is continued until the turbidity thereof reaches a predetermined low level. Meanwhile, the cleansing operation on the second bed is prevented from moving to a third bed until the turbidity of the waste liquid from the first bed reaches the predetermined low level. Such monitor control operation is applied to third and further ports until all filter beds in the system have been cleansed.
A control system for controlling a backwash operation in normal and high flow operating modes is provided in a traveling bridge filter having a filter basin; a filter media bed; a filtrate channel; a traveling bridge adapted to traverse the filter basin with a backwash hood suspended therefrom; a programmable logic controller; a reference sensor and five spaced water level sensors. The controller and the sensors control the backwash operation by sensor functions which differ between the normal and high flow operating modes.