Abstract: Methods and systems for disinfecting conduits using gaseous ozone are disclosed. The systems and methods include an ozone generation apparatus capable of producing gaseous ozone to be introduced into conduits. The gaseous ozone can then disinfect the conduit. Some embodiments of the systems and methods further comprise an ozone destruction apparatus capable of destroying the ozone after a certain stage of the disinfection process is reached.

Abstract: A disinfection reactor for disinfecting liquid, such as water from a water filtration plant, by exposing the liquid to ultraviolet light. The reactor includes a generally rectangular reactor vessel and two or more medium pressure ultraviolet lamps that extend within the reactor vessel in a direction transverse to the direction of liquid flow therethrough. The reactor vessel includes liquid guide surfaces that guide liquid to flow in a converging flow path having a reduced-area flow region in the vicinity of the ultraviolet lamps. The ultraviolet lamps are positioned spaced from and between the guide surfaces.

Abstract: A tubular holder for an actinometric monitoring element for monitoring the irradiance of ultraviolet light within a liquid to be treated for microorganism control. The holder extends into the interior of a vessel or a pipeline that carries a fluid to be treated by exposure to ultraviolet light. A transparent end cap is carried at the end of the holder that is within the vessel or pipeline. Positioned within the holder is an actinometric monitoring element that can be either a transparent container for an actinometric solution or a photocell, each for sensing the irradiance of ultraviolet light emitted by light sources positioned within the vessel or pipeline. The holder is removably received in a sleeve that extends through the wall of the vessel or pipeline.

Abstract: A method and apparatus for disinfecting the interior of pipelines and conduits, particularly water mains. Ozone is utilized as the disinfectant vehicle to neutralize microbial contamination of the conduit. An ozone generation system includes a venturi injector for introducing ozone into pressurized water to provide a treating solution that is introduced into and that flows along a predetermined length of the conduit to be treated. The ozone concentration is regulated to maintain an ozone residual at the conduit outlet of about 0.1 mg/L to about 0.2 mg/L for a time sufficient to assure the desired level of disinfection of the conduit interior.

Abstract: Apparatus for determining the ozone decay rate constant for an ozone-in-water solution. The apparatus includes a single ozone residual sensor, to which a sample flow is directed to measure the initial ozone residual concentration, and to which a delayed flow stream of the same solution is directed to measure the ozone residual concentration after passage of a particular time interval. The time delay of the flow stream is achieved by passing the flow stream through a chamber that includes a tubing coil through which the sample stream flows, after which the ozone residual concentration of the delayed sample stream is measured by the same ozone residual sensor. A portion of the incoming flow stream is diverted to flow through the chamber to maintain the delayed sample stream at substantially the same temperature as the incoming flow stream.

Abstract: A tubular holder for an actinometric monitoring element for monitoring the irradiance of ultraviolet light within a liquid to be treated for microorganism control. The holder extends into the interior of a vessel or a pipeline that carries a fluid to be treated by exposure to ultraviolet light. A transparent end cap is carried at the end of the holder that is within the vessel or pipeline. Positioned within the holder is an actinometric monitoring element that can be either a transparent container for an actinometric solution or a photocell, each for sensing the irradiance of ultraviolet light emitted by light sources positioned within the vessel or pipeline. The holder is removably received in a sleeve that extends through the wall of the vessel or pipeline.

Abstract: A chemical actinometer for determining the absolute level of exposure to ultraviolet light of a fluid to be treated for disinfection purposes. The actinometer includes a translucent sample cell through which the chemical actinometric fluid flows. The area of exposure of the actinometric fluid is controlled by allowing the ultraviolet light to pass through only a portion of the sample cell. A suitable actinometric fluid is a combination of iodide and iodate in a solution. The sample cell is positioned within an ultraviolet disinfection reactor at a position to receive ultraviolet light from the ultraviolet light source.

Abstract: A chemical actinometer for determining the absolute level of exposure to ultraviolet light of a fluid to be treated for disinfection purposes. The actinometer includes a translucent sample cell through which the chemical actinometric fluid flows. The area of exposure of the actinometric fluid is controlled by allowing the ultraviolet light to pass through only a portion of the sample cell. A suitable actinometric fluid is a combination of iodide and iodate in a solution. The sample cell is positioned within an ultraviolet disinfection reactor at a position to receive ultraviolet light from the ultraviolet light source.

Abstract: A device for introducing ozone uniformly into water flowing through a conduit for disinfecting the water. An ozone-contacting vessel is provided and includes a downflow tube through which water is caused to flow. The downflow tube is positioned vertically within a diffusion chamber. Within the downflow tube are a plurality of layers of transversely extending porous elements that are in communication with a source of ozone to provide a relatively uniform distribution of fine ozone bubbles over the cross-sectional area of the downflow tube. The downflow tube can be J-shaped, to convey ozonated water into downstream ozone reaction cells to permit oxidation or disinfection of the water being treated. An outlet seal plate is provided at the J-tube outlet to prevent backflow into the J-tube upon shutdown of the contactor cell containing the J-tube.

Abstract: A device for introducing ozone uniformly into water flowing through a conduit for disinfecting the water. An ozone contacting vessel is provided and includes a downflow tube through which water is caused to flow. The downflow tube is positioned vertically within a diffusion chamber. Within the downflow tube are a plurality of layers of transversely extending porous elements that are in communication with a source of ozone to provide a relatively uniform distribution of fine ozone bubbles over the cross-sectional area of the downflow tube. The porous elements are carried by an ozone conduit that is substantially coaxially positioned within the downflow tube. Spacer members are provided to space the porous elements from the downflow tube wall, and the entire ozone distributor assembly can be easily removed form the downflow tube for servicing the porous elements and can then be easily reinstalled thereafter.

Abstract: A gravity flow, single or multi-cell filter incorporating an integral backwash control chamber for enabling backwashing to occur without the need for backwash pumps. The backwash control chamber contains a volume of backwash liquid, and communicates with a source of pressurized backwash liquid through a float-controlled flow control valve in order to maintain a desired liquid level within the backwash control chamber during backwashing operations. The flow of backwash liquid from the backwash control chamber is controllable either by means of three-way valves interconnecting the backwash control chamber with the filter outlet chamber, or by wash water control gates within the backwash chamber that are adapted to selectively cover outlet openings to permit backwash flow to enter the filter outlet chamber.

Abstract: Apparatus and a method for disinfecting water by contacting the water with gaseous ozone. The device includes a series of treatment chambers that are interconnected serially by external transfer conduits, each transfer conduit including an introduction tap for introducing ozonated water into the water to be treated. The treated water flows sequentially from one chamber into the next. Hydrogen peroxide is added to the water as it enters a final chamber for final degasification of the water. Within each treatment chamber a mixing chamber is provided for additional intermixing and greater mass transfer of ozone with the water by alternately speeding up and slowing down the flow of the ozone-water mixture before the mixture is introduced downwardly into the respective chamber adjacent the lower wall thereof.

Abstract: A multiple filter, gravity flow, liquid filtering apparatus includes a plurality of adjacent independent filter chambers with common influent and effluent passages surrounding a centrally located effluent control chamber and having provisions for backwashing at least one filter chamber with the effluent from companion filter chambers. The effluent control chamber preferably has two sections, a lower section which serves to collect filtrate from each of the surrounding filter chambers through a plurality of flow transfer ports which communicate with each filter chamber, and an upper section which houses equipment and controls for filtering and backwash operations. In one embodiment, the lower section includes a vertically disposed outlet conduit with an adjustable weir located at the open end of the conduit. The weir is used to adjust the liquid level in the lower section of the control chamber to control filtering and backwash operations.

Abstract: A coarse media flocculator utilizes buoyant media restrained against upward movement in a flocculator chamber whose cross-sectional area increases uniformly in the direction of vertical flow, thereby providing a uniformly tapering velocity gradient. The height of the media bed within the chamber is alterable, thereby changing its depth and cross-sectional characteristics within the tapered chamber. The velocity gradients of the flocculator can thus be changed independent of flow. The media restrainer comprises interlocked cooperating gratings each respectively joined to an opposite wall of the flocculator housing by a tracking mechainsm. Upon manipulation of a motor device, one grating is horizontally extended or retracted, producing a lowering or raising of the restrainer as its cross-sectional area is respectively enlarged or reduced.

Abstract: A sedimentation process for the collection and removal of solid particles from a liquid includes a basin provided with a plurality of planar baffles or settler members each having opposite ends attached to support rods, with the latter obviating the need for any beams or the like, to support the lower edges of the settler members. Manipulation of an adjustment mechanism permits simultaneous alteration of the inclination of all of the settler members without halting operation of the process. Influent is directed into the basin through a plurality of ports spaced longitudinally of one side wall thereof to more evenly distribute the influent throughout the bottom expanse of the settler members. Preferably, the settler members comprise stretchable membranes with the support rods including a shiftable, lockable mechanism permitting quick installation and variation of the tension as applied to the settler members.

Abstract: A coarse media flocculator utilizes buoyant media restrained against upward movement in a vertical chamber whose cross-sectional area increases uniformly in the direction of flow, thereby providing a uniformly tapering velocity gradient. The height of the media restrainer within the chamber can be adjusted, thereby changing the depth and cross-sectional characteristics of the media bed within the tapered chamber. The velocity gradients of the flocculator can thus be changed independent of flow. A washwater piping grid with downwardly pointed jet spray nozzles is positioned within the media bed for cleaning. The height of the media bed can be adjusted by changing the position of the media restrainer or by changing the liquid level within the chamber, thus changing that part of the media bed where the jet spray is concentrated. In one embodiment, the restrainer is disposed within an area of the chamber above the tapered portion having a uniform cross-section.