REACTOR
20210197945 · 2021-07-01
Inventors
- Svenja Bierbaum (Hamburg, DE)
- Joerg Grube (Escheburg, DE)
- Wiebke Matthias (Hamburg, DE)
- Pascal Philippsen (Hamburg, DE)
- Andreas Thiele (Hamburg, DE)
- Juergen Wetzel (Hamburg, DE)
Cpc classification
C02F2103/008
CHEMISTRY; METALLURGY
International classification
B63J4/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A reactor configured to clean ballast water on ships includes a reactor housing having an inlet and an outlet and a reactor tube in the reactor housing providing a fluid connection between the inlet and the outlet. The reactor tube includes an inner wall having a plurality of rounded recesses extending longitudinally from a first end of the reactor tube to a second end of the reactor tube, and the rounded recesses each have a substantially constant cross section from the first end of the reactor tube to the second end of the reactor tube. A radially inwardly projecting ridge extends between each circumferentially adjacent pair of the rounded recesses.
Claims
1-8. (canceled)
9. A reactor configured for cleaning ballast water on ships comprising: a reactor housing having an inlet and an outlet, a reactor tube in the reactor housing providing a fluid connection between the inlet and the outlet, the reactor tube including an inner wall having a plurality of rounded recesses extending longitudinally from a first end of the reactor tube to a second end of the reactor tube, wherein the rounded recesses each have a substantially constant cross section from the first end of the reactor tube to the second end of the reactor tube, and wherein a radially inwardly projecting ridge extends between each circumferentially adjacent pair of the rounded recesses.
10. The reactor according to claim 9, including an elongated treatment device located at least partially in each of the plurality of rounded recesses.
11. The reactor according to claim 10, wherein the rounded recesses are uniformly distributed in the circumferential direction.
12. The reactor according to claim 10, wherein more than half a surface area of the inner wall is located in the plurality of recesses.
13. The reactor according to claim 10, wherein a first end of the reactor housing includes a plurality of end-side receptacles each configured to receive an end of one of the plurality of elongated treatment devices.
14. The reactor according to claim 13, wherein a subset of the plurality of receptacles are arranged in a ring.
15. The reactor according to claim 10, including a sensor mounted in the reactor tube for recording a measured value.
16. The reactor according to claim 10, wherein at least fifty percent of each of the plurality of treatment devices is located in a respective one of the plurality of recesses.
17. The reactor according to claim 10, including a sensor mounted in the reactor tube for recording a measured value, wherein the rounded recesses are uniformly distributed in the circumferential direction, wherein more than half a surface area of the inner wall is located in the plurality of recesses, wherein a first end of the reactor housing includes a plurality of end-side receptacles each configured to receive an end of one of the plurality of elongated treatment devices, wherein a subset of the plurality of receptacles are arranged in a ring, wherein at least fifty percent of each of the plurality of treatment devices is located in a respective one of the plurality of recesses, and wherein the treatment devices comprise ultraviolet lamps.
18. The reactor according to claim 10, wherein, in cross section, each of the recesses extends radially outwardly from a side of an imaginary regular polygon.
19. The reactor according to claim 18, wherein the polygon is a pentagon.
20. The reactor according to claim 18, wherein each side of the imaginary polygon intersects one of the plurality of elongated treatment devices.
21. The reactor according to claim 10, wherein the elongated treatment devices comprise ultraviolet lamps.
Description
[0015] In the following, a preferred starting example of the invention is explained in more detail with reference to schematic illustrations.
[0016]
[0017]
[0018]
[0019] 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.
[0020] According to
[0021] 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.
[0022] 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 (
[0023] 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.
[0024] 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 (
[0025] Further treatment devices 36a, 36b are disposed centrally along the reactor tube longitudinal axis x between the treatment devices 30a to 30e (
[0026] 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.
[0027] 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.
[0028] 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/m.sup.2. 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.
[0029] 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.
[0030] 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.
REFERENCE NUMBER LIST
[0031] 2 Reactor [0032] 4 Reactor housing [0033] 6 Separating wall [0034] 8 Inner space [0035] 10 Inner space [0036] 12 Cover [0037] 14 Cover [0038] 16 Inlet [0039] 18 Emptying device [0040] 19 Outlet [0041] 20 Emptying device [0042] 22 Opening in separating wall [0043] 22 Reactor tube [0044] 24a to 24e Recess [0045] 25 Elevation [0046] 26 Recess-side inner-circumferential section surface [0047] 28 Inner-circumferential section surface between recesses [0048] 30a to 30e Treatment devices [0049] 32 UV receptacle [0050] 34 UV receptacle [0051] 36a, b Treatment devices [0052] 40 UV receptacle [0053] 42 UV receptacle [0054] 44 Sensor [0055] 46 Sensor tube [0056] 48 Opening in the reactor tube [0057] x Reactor tube longitudinal axis