Fluid treatment system and method of treating fluid

Radiant energy – Fluent material containment – support or transfer means – With irradiating source or radiating fluent material

Reexamination Certificate

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C250S373000, C422S186300, C422S024000, C422S906000

Reexamination Certificate

active

06803586

ABSTRACT:

BACKGROUND OF THE INVENTION
1. Field of the Invention
In one of its aspects, the present invention relates to a fluid treatment system, more particularly an ultraviolet (UV) water treatment system in an open channel, the performance of which is improved by mitigating flow through the low intensity region of the reactor above the top lamp when the system is operated at high fluid velocities. In another aspect of the invention, this is achieved by designing elevation differences between the upstream and downstream ends of the system while obviating or mitigating top lamp overheating due to exposure during periods of low flow.
2. Description of the Prior Art
UV disinfection systems are used in wastewater and drinking water plants to control microbial growth. UV of a wavelength which can be absorbed by cellular nucleotides causes cross-linking, or dimerization, of RNA and DNA, preventing the micro-organisms from replicating and effectively disinfecting the water (Jagger, J.
Introduction to research in ultraviolet photobiology
. Englewood Cliffs, N.J.: Prentice-Hall Inc., 1967; p.69-73). This technology has been successfully applied commercially in large scale systems since 1981 (U.S. Pat. No. 4,482,809).
Open channels are commonly used to transport or convey large volumes of fluid by gravity and are typically made of concrete. Gravity is used to avoid the high pumping costs that would be incurred if the transport channels were closed and pressurized. Routine cleaning maintenance is made easier by having access to the channel through the open top. Thus, in some applications, it is advantageous when designing a UV disinfection system to make use of conventional open fluid channels to minimize reactor costs and provide for ease of maintenance while still maintaining a gravity flow regime to avoid incurring pumping cost.
Open channel UV disinfection systems for water treatment typically consist of a number of modular assemblies (also known as radiation source modules) arranged in parallel across the width of the fluid canal (U.S. Pat. No. 4,482,809, copending U.S. patent application Ser. No. 09/185,813 (filed Nov. 3, 1998) and copending U.S. patent application Ser. No. 09/258,143 (filed Feb. 26, 1999)). An example of such an assembly is shown in FIG.
1
. These assemblies may consist of a number of radiation source modules (
1
), such as UV lamps enclosed in quartz sleeves, that are substantially parallel to the direction of fluid flow. The modules may be lifted from the channel for routine maintenance, such as sleeve cleaning and lamp replacement. In some cases, an automatic cleaning mechanism is present, consisting of a wiper canister (
2
) and a drive mechanism (
3
). The fluid flows past the modules in a relatively unrestricted fashion under the influence of gravity, with a minor difference in water level between the upstream and downstream ends required to allow the water to pass the submerged geometry. This water level difference is dependent on a number of factors, including the complexity of the submerged geometry, the horizontal spacing between modules, the fluid velocity and the like.
The effectiveness of an open channel UV system depends on its ability to deliver the dose of UV required to reach the target disinfection level to each fluid element. The UV dose is defined as the product of UV intensity and reactor retention time, and is normally expressed in mWs/cm
2
. The inactivation of micro-organisms follows a first order kinetic expression proportional to the UV dose (Jagger, J.
Introduction to research in ultraviolet photobiology
. Englewood Cliffs, N.J.: Prentice-Hall Inc., 1967; p.69-73). Therefore, the delivery of a uniform dose to all micro-organisms as they pass through the reactor improves reactor efficiency.
As UV passes through a fluid, its intensity at a given point depends on the fluid transmittance of the wavelength in question. The most common germicidal wavelength used is 254 nm, since this wavelength is produced effectively by conventional low pressure mercury arc lamps. Wastewater often exhibits low transmittance of germicidal wavelengths, resulting in a decrease in UV intensity as light travels away from the lamps. This leads to regions of lowest UV intensity between lamps. A certain spacing, dependent on water quality and lamp type is desirable to ensure adequate dose delivery and reactor performance.
The residence time required for adequate dose delivery depends on UV intensity. For poor water quality, UV transmittance and average UV intensity are low, usually requiring relatively long residence times within the reactor to maintain adequate dose. This is typically accomplished by designing the UV disinfection system with banks of UV modules disposed serially. Conversely, with good water quality or high intensity radiation sources, residence time is normally decreased to achieve the same dose. This is usually accomplished by designing relatively narrow fluid channels, decreasing the amount of UV equipment required as compared with a system installed in a wide channel. This results in relatively high fluid velocities past the modules, leading to significant differences in water level between the upstream and downstream ends of the system.
Since UV radiation from each lamp only penetrates a certain distance into the fluid, each lamp can effectively treat a layer of water around it, usually equal to approximately one half the spacing between lamps. When large water level differences cause the layer of water above the top lamp to exceed this critical value, the excess water travels through a zone of relatively low UV intensity, exiting the irradiation zone with lower than adequate dose. This fluid “short circuit” leads to non-uniform dose distribution, resulting in micro-organisms escaping essentially untreated, leading to poor overall reactor performance.
It is desirable to have a reactor which obviates or mitigates water level differences that lead to a “short circuit” above the top lamp over a relatively wide range of water qualities and flow rates. The submerged geometry is fixed by the design of the modular assemblies and usually cannot easily be modified without comprising equipment functionality. Horizontal spacing often cannot be increased without producing regions of low UV intensity in the reactor. For good water quality or high intensity radiation sources, it is therefore usually important to operate a UV disinfection system at high fluid velocities for the reasons described above.
It would be desirable to have a fluid treatment system capable of obviating or mitigating a “short circuit” effect over the top lamp of a UV disinfection system when operated at high fluid velocities using elevation differences between the upstream and downstream ends of the reactor.
SUMMARY OF THE INVENTION
It is an object of the invention to provide a novel fluid treatment system which obviates or mitigates at least one of the above-mentioned disadvantages of the prior art.
Accordingly, in one of its aspects, the present invention provides a fluid treatment system comprising at least one radiation source disposed in an open irradiation zone, the irradiation zone have a fluid inlet which is elevated with respect to a fluid outlet.
In another of its aspects, the present invention provides a fluid treatment system comprising an array of radiation sources disposed in an open channel, an upstream end of the open channel adjacent an upstream end of the array being elevated with respect to a downstream end of the open channel adjacent a downstream end of the array.
In yet another of its aspects, the present invention provides a fluid treatment system comprising a first irradiation zone and a second irradiation zone disposed at different heights with respect to one another such that the fluid level is substantially normalized with respect to the top of each of the first irradiation zone and the second irradiation zone.
In yet another of its aspects, the present invention provides a fluid treatment system comprising a plurality of serially disposed irradiation zones which

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