System separation device
11053669 · 2021-07-06
Assignee
Inventors
Cpc classification
E03C1/10
FIXED CONSTRUCTIONS
C02F2201/3221
CHEMISTRY; METALLURGY
E03B7/078
FIXED CONSTRUCTIONS
C02F2307/14
CHEMISTRY; METALLURGY
Y02A20/20
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
E03B7/07
FIXED CONSTRUCTIONS
Abstract
A system separation device with at least one pressure-proof tank for containing a liquid that forms a predetermined liquid level in the tank, above which level there is a gas cushion. The device contains an inlet in the upper region of the tank for fluidly feeding the tank from a first fluid system, and an outlet in the lower region of the tank for forwarding the liquid to a second fluid system. To prevent the germ-infestation of the inlet, at least one germicide material is arranged in the region of a gas cushion above the liquid level.
Claims
1. A system separation device configured to be attached to a source of drinking water and comprising: a tank having a bottom and configured to hold liquid up to a predetermined liquid level in the tank, a gas inlet configured to deliver a flow of gas, under constant pressure, into the tank to fill a volume about the predetermined liquid level with gas and to prevent liquid in said tank from rising above the predetermined liquid level, a drinking water inlet in an upper region of the tank, said drinking water inlet configured to feed, in operation of the device, the tank with the drinking water from said source such that pressure of said gas in the volume is defined by operation of said drinking water inlet, a liquid outlet in a lower region of the tank, said outlet configured to forward the liquid from the tank, a UV light source disposed in operation of the separation device wholly above the predetermined liquid level and in said volume and configured to irradiate the drinking water inlet with UV light to prevent contamination of said drinking water inlet with contaminants located below said drinking water inlet to microbiologically separate said drinking water from said liquid held in the tank, and a receiving pot disposed in the tank below the drinking inlet to receive a flow of the drinking water falling down from the drinking water inlet into the tank and to absorb a kinetic energy of said flow.
2. The system separation device according to claim 1, wherein the tank has at least one filling level sensor configured to determine a level of liquid filling the tank during the operation thereof.
3. The system separation device according to claim 1, wherein the UV light source is configured to irradiate an annular region of an inner side of a wall of the tank, wherein the annular region is dimensioned to surround the drinking water inlet.
4. The system separation device according to claim 1, wherein the gas filling said volume comprises a germicidal gaseous substance at a first concentration that is higher than a second concentration, the second concentration being a concentration of said germicidal gaseous substance in air.
5. The system separation device according to claim 1, wherein a wall of the tank satisfies at least one of the following conditions: a) the wall contains a coating at at least one of (i) the inner side of the wall, (ii) a region of the drinking water inlet, and (iii) around the region of the drinking water inlet, wherein said coating includes a germ-inhibiting or germicidal material, and b) said wall consists of germ-inhibiting or germicidal material.
6. The system separation device according to claim 5, wherein the inner side carries a semiconductor material dimensioned as annular region on the inner side, and wherein a band gap of the semiconductor material is smaller than energy of photons emitted by the UV light source during operation thereof.
7. The system separation device according to claim 6, wherein the semiconductor material comprises titanium oxide (TiO.sub.2).
8. The system separation device according to claim 1, wherein the tank contains a non-water-soluble germicidal fluid substance, wherein a density of said substance is lower than a density of water.
9. The system separation device according to claim 1, wherein the tank has a release valve, a release opening below the predetermined liquid level configured to be controlled by the release valve, and a controller configured to open the release valve when said predetermined liquid level cannot be maintained in operation of the device.
10. The system separation device according to claim 9, wherein the controller is configured to monitor the operation of the system separation device and, in an event of a malfunction, to open the release opening and the inlet.
11. The system separation device according to claim 1, wherein the tank comprises a ventilation device.
12. The system separation device according to claim 1, further comprising: a sensor system configured to detect a distance separating a level of liquid, filling the tank, and the drinking water inlet, a compressor configured to deliver said flow of gas at said constant pressure into the tank, and a control circuitry configured to activate the compressor when the distance, detected by the sensor system, falls below a nominal value.
13. The system separation device according to claim 1, wherein a rim of the receiving pot is disposed above the predetermined liquid level.
14. The system separation device according to claim 1, wherein the UV light source is disposed to be separated from the liquid in said tank during the operation of the device.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) In the following, the invention will be described by way of example, without limitation of the general inventive concept, on examples of embodiment and with reference to the drawings.
(2)
(3)
(4)
DETAILED DESCRIPTION
(5)
(6) The tank 10 is formed of a pressure-resistant material. This is preferably a hygienically acceptable material, such as e.g. stainless steel or the like.
(7) Furthermore, the system separation device 1 has a liquid inlet 20 into the tank 10. Via the liquid inlet 20, a liquid, e.g. drinking water is fed into the tank 10. As shown in
(8) As shown in
(9) A liquid outlet 30 is located in the lower part of the tank, i.e. below the liquid level (preferably near the bottom). The liquid 2 present in the tank 10 is delivered via the liquid outlet 30 to a drinking water or industrial water system or the like, i.e. to a consumer in general.
(10) As shown in
(11) Furthermore, the system separation device 1 has a ventilation device 40. It is connected to the tank 10 between the liquid inlet 20 and liquid outlet 30 and ensures that the tank level does not fall below a minimum tank level B.sub.min.
(12) The term tank level generally refers to the height of the liquid level W in the tank, i.e. the distance of the liquid surface from an inner surface 12i of the bottom wall 12 facing towards the tank interior 10i, and in particular a lowest point of the inner surface 12i of the bottom wall 12 with respect to the direction of gravity G.
(13) The minimum tank level B.sub.min depends on device-specific provisions. For example, it can be provided that, depending on the liquid requirement of the consumers connected to the system separation device, a certain amount of liquidwhich causes a certain tank levelmust not be dropped below in the tank, such that the supply of the consumers is ensured.
(14) As shown in
(15) Preferably, the venting device 40 may have an automatic venting valve with at least one float as a level sensor. Particularly advantageously, two redundant venting valves 41, 42 are controlled, i.e. opened or closed upon controlling by floats or the like. This increases the reliability of the system.
(16) As shown in
(17) It is preferably provided that the level sensor 14 detects at least a maximum tank level B.sub.max. The tank level B.sub.max is defined by a minimum permissible distance d.sub.min between the liquid level and the liquid inlet 20. This minimum distance d.sub.min must be chosen such that the passage of bacteria, germs, contaminations and the like from the medium/liquid in the tank 10 into the water inlet 20 is excluded. Preferably, d.sub.min is more 3-times the inner diameter of the supply pipe 21, and particularly preferred more than 6-times the inner diameter of the supply pipe 21.
(18) As shown in
(19) To increase safety, also several level sensors can be provided. For example, as shown in
(20) As shown in
(21) Should for any reason the regulation of the level sensors 14, 15 be defective, the emergency opening valve 81 ensures that the liquid level W cannot rise so far that the minimum distance d.sub.min is not maintained. Thus, the hygiene region is triple-protected. Even in case of power failure, the minimum distance d.sub.min is guaranteed. The overflow of the emergency opening valve 81 may end in an optional safety basin 60.
(22) The level sensors 14, 15 can be designed as touch probes, floats, ultra-sonic probes or the like.
(23) As already described, there is a gas cushion as the hygiene zone L between the medium/liquid in the tank 10 and the upper tank end, which gas cushion is under the pressure p.sub.zu of the liquid inlet 20 being established in the tank interior 10i. The gas cushion and thus also the hygiene zone L extend in particular between the liquid surface and the top wall 13 of the tank 10. In order to keep the pressure of the gas cushion/hygiene zone L constant, the system separation installation 1 has a gas generating device. As shown in
(24) The pressure generating device 50 has a gas supply device 51 opening into the tank interior 10i. The pressure generating device 50 ensures that the gas cushion is always under a constant pressure, i.e. any gas losses are compensated by the pressure generating device 50. This prevents the depletion of the gas cushion, which would cause the liquid level W to rise. In this way, it is excluded that the minimum distance d.sub.min between the liquid level and the liquid inlet 20 is not maintained. A migration of germs from the medium/liquid which is located in the tank 10, to the medium/liquid, which is located in the liquid inlet 20 is prevented with extremely high reliability by means of the system separation installation of
(25) Due to the pressure p.sub.zu of the liquid inlet 20 lying above the atmospheric pressure, the system separation device 1 of the invention can do without additional pumps, since the liquid is not depressurized and the inlet does not communicate with the atmosphere. Thus, the system separation device (
(26) In order to keep the pressure in the hygiene zone L at least substantially constant, it can be provided that the pressure generating device 50 feeds a gas, e.g. air, via a gas supply device 51 to the tank interior 10i.
(27) As shown in
(28) A compressor or other gas generating method may be provided as the pressure generating device 50. This can be directly connected to the tank 10 via the gas supply device 51. Advantageously, the compressor may also feed a storage tank (not shown) which is connected to the tank 10 via the gas supply device 51. This has the advantage that pressure variations of the air cushion L within a certain range, in particular small pressure variations, can be compensated by supplying gas from the storage tank into the tank 10, without further gas supply by the compressor into the storage tank being necessary.
(29) As further shown in
(30) In order to ensure the sterility of the tank interior 10i, the liquid outlet 30 can furthermore have a check valve 32, as shown in
(31)
(32) The inlet 20 may have a check valve 22 which is connected to the inlet in such a way that the check valve 22 permits only one flow direction S20 of the water into the tank interior 10i. This prevents that water can flow back from a section 21a of the water supply pipe 21, which section 21a is located upstream of the check valve 22 when seen from the tank 10) into a section 20b of the water supply pipe 21 being located downstream of the check valve 22 when seen from the tank 10. In this way it is ensured that even when the maximum tank level B.sub.max is exceeded, no water from the tank interior 10i, which may be contaminated with germs, can reach the section 20b of the water inlet 20 connected to a fresh water supply.
(33) The system separation device 1 may further comprise a pressure reducer 23 being connected to the water inlet 20. The pressure reducer 23 may be designed as a controllable throttle valve and is preferably located upstream of the check valve 22 with respect to the flow direction S20 being directed into the tank interior 10i. By means of the pressure reducer 23, the pressure p.sub.zu of the water inlet can be adjusted to the desired level.
(34) Furthermore, as shown in
(35) Similar to the water outlet 30, a manometer 25 for reading the pressure in the water inlet 20 can be arranged in the water inlet 20.
(36) In addition, the tank 10 may have a pressure relief valve 70 (safety valve p.sub.max) for discharging gas or medium/liquid 2 from the tank 10. In the embodiment of the system separation device 1 shown in
(37) As further shown in
(38) Preferably, the safety trough 60 may have a leakage sensor 61 which detects when medium/liquid accumulates in the safety trough 60. As a consequence, e.g. when reaching a maximum allowable amount of liquid in the safety trough, the system separation device 1 turns off. In particular, it can be provided that when switching off the system separation device 1, the water inlet 20 into the tank 10 is closed, e.g. by shutting-off the regulated control valve 24.
(39) The system separation device 1 is functionally connected to a control device or circuitry 80 (shortly controller 80) for controlling and regulating the operation of the system separation device.
(40)
(41) The inlet 20 and the outlet 30 each have a valve seat 26, 36, which can be closed by a respective valve body 27, 37, such that the inlet 20 and outlet 30 are shut-off. Accordingly, the valve bodies have an open position in which they release the valve seats 26, 36, and a closed position in which the valve seats 26, 36 are closed. The two valve bodies 27, 37 are connected to one another by an actuating means 90 (here: rod 90), such that always both valve bodies 27, 37 are adjusted synchronously between their corresponding open position(s) and closed position(s). A float (floating body) is attached at the actuating means 90, which presses both valve bodies 27, 37 against their valve seats 26, 36 by means of the actuating means 90 with increasing fluid level in the tank, such that inlet 20 and outlet 30 are closed. This can be reliably prevent that the fluid level increases over a predetermined height in the tank 10, e.g. by fluid flowing back over the outlet. Liquid being eventually contaminated with germs can therefore not reach the inlet. Preferably, at least one of the two valve bodies 27, 37 is biased against the corresponding valve seat (for example, in a direction of the corresponding closed position). The valve in the inlet 20 and/or the valve in the outlet 30 only opens at a corresponding pressure difference. Even low inflow of potentially germ-infested or otherwise contaminated liquid into the tank 10 is excluded, as well as an inflow of potentially contaminated gas or liquid into the inlet 20. Merely in the event that nevertheless the liquid level in the tank should rise above a maximum filling level, the tank has an emergency overflow valve 81. It should preferably be arranged above the float (or floating body) 95. It releases an outlet when the liquid level exceeds the maximum filling level, such that the distance between the liquid level and the inlet decreases below a predetermined value.
(42) The tank 10 has a nominal filling height, the liquid level 3 of which is indicated by a dashed line. Above the nominal filling level is a pressurized gas cushion. The inlet is therefore not in direct contact with the liquid 2 in the tank 10.
(43) In its upper region, the tank 10 can have a gas connection nozzle 53, which is preferably connected to a reservoir for a germicidal gas, with interposition of at least one switching valve. Preferably, the reservoir is under pressure, such that possibly used germicidal gas can be refilled during operation.
(44) If liquid is extracted via the outlet 30 from the lower region of the tank, a corresponding quantity flows in via the inlet. In order that as little as possible of the gas reaches the region of outlet and possibly escapes, the tank has a calming means preferably above the liquid level and/or dipping into the liquid. In the example shown, the calming means is attached to the tank wall and has a trough-shaped recess in the middle. The calming means absorbs the kinetic energy of the liquid inflowing via the inlet. Therefore, no jet penetrates into the liquid 2 deep beneath the liquid level, which jet could entrain gas bubbles to the region of the outlet 30. In the example shown, the calming means is porous, such that water collected above the liquid level can sink steadily and over a large area through the calming means in the direction of the liquid level. Alternatively and/or additionally, the liquid can also flow over the edge of the calming means. In another embodiment, the calming means is a float.
(45) In order to prevent migration along the tank wall in the direction of inlet 20, UV lamps are arranged in the region of the gas cushion, here indicated as rods. They irradiate the tank wall and in particular an annular strip 18 of the tank wall, the surface of which is provided with a germ-inhibiting material or includes such material. Particularly preferred, the germ-inhibiting coating is a semiconductor coating, e.g. of titanium dioxide.
(46)
(47) The system separation device in
(48) The rim 173 is slightly above the intended liquid level 3. It may as well be positioned slightly below or preferably at the intended liquid level 3. In operation the liquid level may vary, but by adding gas via gas inlet 53 or by releasing gas via outlet valve 41, the controller may ensure that the actual liquid level is within predefined boundaries close to the intended liquid level 3. As the liquid flows over the rim, the liquid's flow velocity can be slowed down and in addition the stream is directed towards the gas cushion, enabling gas bubbles to rise upwards and leave the liquid, i.e. to reenter the gas cushion. In short, the receiving pot enables to reduce the flow velocity of the liquid below the velocity with which the bubble rise up in the liquid. The diameter of the receiving pot is preferably larger that than the diameter of the inlet, e.g. twice as big or bigger, to thereby slow the flow over the rim down. The larger the diameter, the slower is the flow velocity of the liquid when passing over the rim and the less are bubbles removed with the liquid flow via the extraction point from the tank. The volume of the gas cushion thus essentially remains constant (assuming a constant pressure in the tank).
(49) The system separation tank 10 of as depicted in
(50) While the invention is susceptible to various modifications and alternative forms, specific embodiments thereof are shown by way of example in the drawings and will herein be described in detail. It should be understood, however, that the drawings and detailed description thereto are not intended to limit the invention to the particular form disclosed, but on the contrary, the intention is to cover all modifications, equivalents and alternatives falling within the spirit and scope of the present invention as defined by the appended claims.
(51) It will be appreciated to those skilled in the art having the benefit of this disclosure that this invention is believed to provide system separation device. Further modifications and alternative embodiments of various aspects of the invention will be apparent to those skilled in the art in view of this description. Accordingly, this description is to be construed as illustrative only and is for the purpose of teaching those skilled in the art the general manner of carrying out the invention. It is to be understood that the forms of the invention shown and described herein are to be taken as the presently preferred embodiments. Elements and materials may be substituted for those illustrated and described herein, parts and processes may be reversed, and certain features of the invention may be utilized independently, all as would be apparent to one skilled in the art after having the benefit of this description of the invention. Changes may be made in the elements described herein without departing from the spirit and scope of the invention as described in the following claims.
LIST OF REFERENCE NUMERALS
(52) 1 system separation device 2 medium/liquid 3 liquid level 10 tank 10i tank interior 11 side wall of the tank 11a recess in the side wall 12 bottom wall of the tank 12i inner face of the bottom wall 13 top wall of the tank 13a recess in the top wall 14, 15 level sensor 16 UV light source 17 calming means e.g. receiving pot 171 side wall of receiving pot 172 bottom of receiving pot 173 rim of receiving pot 18 annular strip 20 liquid inlet 21 liquid supply pipe 21a, 21b sections of the liquid supply pipe 22 check valve 23 pressure reducer 24 regulated control valve 25 manometer 26 valve seat 27 valve body 30 liquid outlet 30a section of the liquid outlet 31 drain pipe 32 check valve 33 manometer 36 valve seat 37 valve body 38 second outlet/release outlet 39 second outlet control valve/release valve 40 ventilation device 41, 42 ventilation valves 50 pressure generation device 51 gas supply device 52 regulated shut-off valve 53 gas connection nozzle 60 safety trough 61 leakage sensor 70 pressure relief valve 80 regulation/control 81 emergency overflow valve 85 switching valve 85 switching valve 90 actuation means/rod 95 float or floating body