The present invention relates to a reactor for the cleaning of liquids, in particular of ballast water on ships, according to the preamble of patent claim 1.
For improved stabilization, ships regularly take in ballast water and release it again as necessary. The ballast water is directly removed from the body of water, filtered, freed of microbes, microorganisms, and the like or disinfected according to statutory provisions, and subsequently stored in a ballast water tank. The disinfecting is usually effected in a reactor by a treatment with ultraviolet radiation (UV radiation) and/or with ultrasound waves (US waves). During return of the ballast water into the body of water, the ballast water is guided through the reactor again and disinfected again. However, a filtering is not necessarily provided then.
Known reactors for the cleaning of ballast water have a reactor housing that includes a liquid inlet and a liquid outlet. A reactor tube is disposed in the reactor housing that produces a fluid connection between the liquid inlet and the liquid outlet. The reactor housing has a cylindrical inner wall and is penetrated axially by a variety of elongated treatment devices such as UV lamps. In addition, at least one US rod sonotrode is usually provided that extends into the reactor tube.
It is the object of the invention to provide a reactor with an improved cleaning effect.
This object is achieved by a reactor having the features of patent claim 1.
An inventive reactor for the cleaning of liquids, in particular of ballast water on ships, has a reactor housing that includes a liquid inlet and a liquid outlet. In the reactor housing a reactor tube is disposed that produces a fluid connection between the liquid inlet and the liquid outlet. According to the invention the reactor has at least one recess on its inner wall for sectional receiving of a treatment device. The recess has an elongated or groove- or channel-type design and extends over the entire length of the reactor tube. An exemplary treatment device is an elongated lamp that emits ultraviolet radiation (UV). Due to the arrangement of a treatment device in the at least one inner-wall-side recess, the cleaning effect improves compared to a conventional reactor including a reactor tube having a cylindrical inner wall.
The at least one recess is preferably rounded. It is configured as a concave hollowing-out of the inner wall. Due to this measure, unfavorable flow conditions through the recesses are prevented. In addition, it is thereby achieved that the recess-side inner-wall-section surface is guided around the treatment device at a constant spacing, which further improves the cleaning effect since the recess-side inner-wall-section surface has the same spacing from the treatment device over its entire circumferential and axial extension.
Furthermore, the cleaning effect can be improved by a variety of recesses being provided, each for receiving a treatment device. A variety of, for example, UV lamps can thereby be disposed in the reactor so that the UV treatment is effected over the entire flow cross-section of the reactor tube.
For homogenization of the treatment it is preferred when the recesses are uniformly distributed over the inner wall in the circumferential direction.
If in the circumferential direction of the reactor tube the sum of the inner-wall-section surfaces between the recesses is smaller than the sum of the recess-side inner-wall-section surfaces, shadow spaces or shadowing can be prevented, whereby the cleaning effect is further improved.
The reactor housing can have end-side receptacles for receiving the treatment devices, wherein some of the receptacles are disposed in a ring and at least one of the recesses is positioned in the center between the annularly disposed receptacles. A further treatment device can be introduced into the central recess so that the number of the first treatment device such as UV lamps can be further increased, or a different type of treatment device, for example, an ultrasound rod sonotrode (US sonotrode) can be introduced into the reactor tube so that a second treatment method can be carried out for the disinfecting. Since the receptacle is centrally disposed, it is ensured that the treatment of the ballast water is effected over the entire flow cross-section of the reactor tube.
In order to check an effect of the treatment or for adjusting of the treatment devices, for example, with respect to their radiation power/dose/intensity or their number to be activated, it can be advantageous to record a measured value in the ballast water in the reactor tube. For example, the sensor can be configured to determine the permeability of UV radiation or the spread of sound waves due to a US bombardment. In order not to impede the treatment, it is preferred when a sensor provided for this purpose is radially insertable into the reactor space.
A preferred reactor has a variety of treatment devices that are adapted to the respective recess such that they are received in the recess with more than 50% of their cross-sectional surface. The treatment devices are thereby each extensively disposed in the respective recess, which further improves the cleaning effect.
Other advantageous exemplary embodiments of the invention are the subject matter of further dependent claims.
In the following, a preferred starting example of the invention is explained in more detail with reference to schematic illustrations.
Before the introducing of the ballast water into the reactor housing 2, it is filtered in a not-shown filter, for example, having a mesh width of 20 μm. Contaminants and microorganisms ≥20 μm are thereby removed. The filtering is effected during receiving of the ballast water, but not necessarily during removal of the ballast water from a ballast-water tank. The filter device operates continuously.
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The inner spaces 8, 10 preferably each have a flow cross-section that is substantially larger, for example, approximately twice as large, as the flow cross-section of the reactor tube 22. A slowdown of the liquid to be treated in the inner spaces 8, 10 thereby occurs. The inlet 16 and the outlet 18 preferably have a uniform flow cross-section that is the same as or nearly equal to the flow cross-section of the reactor tube 22.
The reactor tube 22 is open on its two end sides over its entire flow cross-section. The ballast water thus enters axially into the reactor tube 22, flows through it axially and exits axially from the reactor tube 22. The reactor tube 22 is closed on the circumference. This has the advantage that the ballast water exclusively flows axially along the treatment device. The ballast water only experiences a redirecting in the opening region and escape region of the reactor tube 22 and impacts perpendicularly against the treatment device. The reactor tube 22 has an inner wall that is provided with a variety of elongated recesses 24a to 24e uniformly distributed over the circumference (
The UV lamps continuously emit UV light within a preferred wavelength range of 200 nm to 400 nm at various intensities. Since different microorganisms absorb different wavelengths, this range makes it possible to account for and to deactivate a variety of microorganisms.
The treatment devices 30a to 30e extend over the entire length of the reactor tube 22 and emerge from the covers 12, 14 at the ends in a fluid-tight manner through corresponding openings 32, 34. They are each radially rejected from the recess-side inner-circumferential-section surfaces 26. Here their positioning in the recesses 24a to 24e is such that the recess-side inner-circumferential-section surfaces 26 are guided around the respective treatment device 30a to 30e at a constant spacing (
Further treatment devices 36a, 36b are disposed centrally along the reactor tube longitudinal axis x between the treatment devices 30a to 30e (
The treatment with ultrasound causes high-pressure phases (compression) and low-pressure phases (rarefaction). Vapor-filled microbubbles, so-called cavities, in the liquid expand in the low-pressure phase and are compressed in the high-pressure phase, which ultimately causes a destruction of the microbubbles within milliseconds. A large amount of energy is thereby released, which in turn allows local high temperatures and pressure waves to arise. The high temperatures effect, for example, a denaturing of the enzymes and proteins. The pressure waves cause, for example, damage to the zooplankton. The ultrasound bombardment is effected continuously. A preferred frequency spectrum falls in the range wherein physical/mechanical effects of the ultrasound bombardment overlap. This is in the low-frequency range wherein cavity formation is more pronounced than in the high-frequency range at approximately 500 kHz. A low-frequency range falls, for example, around 20 kHz. Large bubbles, large pressure pulses, and high temperatures arise during collapsing of the bubbles. Physical/mechanical effects thus dominate that have a destructive effect on particles and microorganisms. The effect of the US treatment also depends on the ultrasound dose, which can be varied.
Due to the combination of the UV treatment and the US treatment, the disinfecting effect on the microorganisms is increased. The risk of the reactivating of the microorganisms is thereby significantly reduced or even avoided. A combined treatment is also more effective than an individual treatment only with ultraviolet radiation or with ultrasound waves.
For recording a measured value in the liquid, a sensor 44 is provided that is disposed in a sensor tube 46. The sensor tube 46 extends radially with respect to the reactor tube longitudinal axis X and penetrates in a fluid-tight manner an unnumbered radial opening in the reactor housing 4 as well as a radial opening 48 in the reactor tube 22, wherein it terminates flush with a recess-side inner-circumferential section surface 26. Here the sensor 44 is, for example, a UV sensor, using which a permeability of the ballast water for the UV radiation is measured. The permeability can serve for adjusting and controlling the treatment devices 30a to 30e, 36a, 36b. The measurement range of the sensor 44 is adapted to the UV lamps. Its measurement range is preferably 0 to 1000 W/m2. Viewed in the flow direction, the sensor 44 is preferably located behind the separating wall 6. It is thus disposed behind the reactor tube center, so that the sensor tube 46 extends through the rear inner space 10.
It should be noted that in principle there is also the possibility to carry out a treatment of the ballast water directly in the inner spaces 8, 10. In the inlet-side inner space 8, a pretreatment could thus be effected, and a post-treatment could be effected in the outlet-side inner space 10. The “core treatment” would then be effected in the reactor tube 22. For this purpose corresponding treatment devices, for example, US sonotrodes 36a, 36a could be used in corresponding receptacles of the cover 12, 14. In particular, different types of treatment, for example, UV treatment or US treatment, or the same treatment could be effected, but with different power/intensity/dosage. For example, since the outlet-side inner space 10 has a larger axial extension than the inlet-side inner space 8, longer US rod sonotrodes 36a, 36b are used in the outlet-side inner space 10.
Disclosed is a reactor for the cleaning of liquids, in particular of ballast water on ships, including a reactor housing that includes a liquid inlet and a liquid outlet and wherein a reactor tube is disposed that produces a fluid connection between the liquid inlet and the liquid outlet, wherein on its inner wall the reactor tube includes at least one channel- or groove-type axial cavity for sectional receiving of an elongated treatment device that extends over the entire length of the reactor tube.
Number | Date | Country | Kind |
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10 2018 214 863.5 | Aug 2018 | DE | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2019/071354 | 8/8/2019 | WO | 00 |