• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a method for adjusting the pH of the heating water of a heating system by means of a demineralization device to a target pH in the range between 8 and 10 wherein the heating water is passed through a mixing bed unit containing anion and cation exchangers. In order to be able to carry out an effective adjustment of the pH value in a simple manner, it is provided according to the invention that the heating water is first circulated via the mixed bed unit in such a way that it is brought to a higher pH value and then the heating water via the mixed bed unit in such a way it is circulated that it is acidified to reach the target pH.
    公开号:AT514038A2
    申请号:T50090/2014
    申请日:2014-02-06
    公开日:2014-09-15
    发明作者:
    申请人:Perma Trade Wassertechnik Gmbh；
    IPC主号:
    专利说明:

    1
    The invention relates to a method for adjusting the pH of the heating water of a heating system by means of a demineralizer to a target pH in the range between 8 and 11, wherein the heating water is passed through a mixed bed unit containing anion and cation exchanger.
    The invention also relates to a corresponding device for adjusting the pH of the heating water.
    Practically in every heating water is used as heat transfer medium. This leads to interactions of the water and the water components with the heating materials, with damage caused by corrosion reactions and deposit formation.
    In particular, by increasing the efficiency of heating systems, the heating surface loads (kW / m2) and thus the surface temperatures of the heat transfer surfaces on the water side have been increasingly increased in recent years. This has the consequence that a formation of fouling in the area of flame and flue gas pipes in modern boilers has much greater impact than in older models. Each millimeter of pad thickness results in efficiency losses of up to 15%.
    For these reasons, softened or demineralized water is always used in large plants to prevent the dreaded scale and to largely inhibit possible corrosion processes. In order to ensure the latter, in addition an increased pH must be set and if necessary also chemical inhibitors added.
    What has long been the case for large plants is now being extended to small or very small plants.
    From DE 10 2005 036 356 a device for treating heating water is known. In this case, a water-carrying chamber is used, in which a mixture of acidic and basic ion exchange elements is maintained. For the filling of heating systems, this arrangement is connected to the fresh water network and the heating system to be filled. The fresh water is treated 2/15 2 in the demineralization unit and demineralized, whereby it is converted to a pH in the range between 8 and 11. If the heating water has a pH of ^ 8, the pH value must be increased in a targeted manner until the water reaches the desired target pH value.
    If the starting water is now slightly basic, it must be alkalized to reach the desired target pH.
    For this purpose, then use a corresponding mixture of ion exchange elements in the Mischbetteinheit.
    It would now be desirable to be able to convert both sour and basic source waters to the target pH with a mixed bed unit. This makes handling easy for the installer.
    It is therefore an object of the invention to provide a method of the type mentioned above with which adjusting the pH of the heating water of a heating system is simplified.
    It is another object of the invention to provide a device with which a more effective adjustment of the pH value of the heating water is possible.
    The object of the invention relating to the method is achieved by first circulating the heating water via the mixing bed unit in such a way that it is brought to a high / higher pH and then circulating the heating water via the mixed bed unit in such a way that it is acidified to reach the target pH.
    The mixed bed unit initially acts primarily as an OH supplier with its anion exchangers, thus increasing the pH value of the heating water. If, however, heating water is passed over the mixed bed unit until the anion exchangers are essentially exhausted, the cation exchanger elements continue to deliver H +. 3/15 3
    If the pH of the outlet water is increased, ie the heating water is to be alkalized, then the heating water is led through the mixing bed unit until the anion exchangers are exhausted. This will initially raise the pH further. Subsequently, the pH is lowered again by the H + release of the cation exchanger. When the target pH is reached, the water treatment can then be completed.
    However, it is also possible to use the same method to set heating waters whose pH is more acidic than the desired target pH. Here, simply the pH value of the starting heating water is raised by means of the anion exchanger until the target pH is reached. A preferred embodiment of the invention is such that the mixed bed unit has a higher content of anion exchangers than the cation exchangers. Preferably, between 60 and 70 weight percent anion exchanger and 30 to 40 weight percent cation exchanger are used in the mixed bed unit. With this composition, heating water, either above or below the desired target pH, can be treated as desired. Accordingly, both low and too high pH values in heating systems can be corrected or leveled out. The mixed bed initially acts primarily as an OH supplier and increases the pH value of the heating water. By controlling the mixing bed in a controlled manner, the pH value can therefore be lowered again, even in the case of strongly basic resin mixtures, in order to reach the pH window required by the heating water guidelines. With the above-described mixing ratios of anion and cation exchangers, in particular target pH values in the range between 8.2 to 8.5 can be set reliably. This range of pH values particularly takes account of heating circuits in which aluminum components are used.
    A possible variant of the invention is such that the heating water is conducted via a main flow line and in parallel via a bypass line, and that the mixed bed unit is arranged in the bypass line. In this way, the inventive method can also during the 4/15 4
    Reliable operation of the heating system. In particular, in the case of an unexpected blocking of the mixed bed, the heating water can continue to circulate over the main flow line. Furthermore, it is also possible that when the target pH value is reached, for example, the water treatment is automatically stopped and, in the process, the heating function continues to be maintained via the main flow line. If by means of corresponding locking elements, the bypass line can be shut off, then an uninterrupted connection or disconnection of the demineralization device can be made.
    It is preferably provided that the mixing bed unit is assigned a pump in the bypass line. This actively promotes a sufficient volume flow through the mixing bed unit, which forms a flow resistance.
    According to a variant of the invention, it may be provided that the mixing bed unit is assigned a flow meter by means of which the heating water flow conducted via the mixing bed unit is measured. With the flow meter, a functional impairment, such as blocking the mixed bed unit can be controlled.
    Furthermore, it is conceivable that the electrical conductivity of the heating water coming from the mixed bed unit is determined with a conductivity sensor arranged downstream of the mixed bed unit. With this conductivity sensor, the ionic slip or thus the degree of exhaustion of the mixed bed can be controlled. In doing so, the knowledge is taken advantage of that, as the duration of the water treatment progresses, first of all the pH value is raised, thereby correlatively lowering the water conductivity. After exhaustion of the anion exchanger then increases again the conductivity of the water. This is accomplished by dispensing ions from the mixed bed into the heating water. This transition point can be determined by means of the conductivity sensor, that is to say the degree of exhaustion of the mixed bed unit can be detected. Consequently, when the degree of exhaustion is reached, the conductivity of the heating water can then be raised again in a controlled manner until the desired temperature is reached
    Target pH (which is correlated with conductivity) is reached.
    A variant of the invention may be such that the pH value of the heating water outside the bypass line is determined, in particular the electrical conductivity of the heating water is measured. If the desired target pH is measured here, the water treatment can be stopped.
    It is particularly preferred that the heating water is only partly desalted by means of the demineralizing device, wherein the salt content is adjusted such that the heating water has an electrical conductivity in the range between 100 pS per cm and 200 pS per cm when the target pH value is reached , In this way, a residual conductivity is left in the water. As a result, a pH buffering effect is achieved by the residual salt content. The heating water is thus insensitive to chemical influences in the set pH range, so that a stabilization of the pH value is possible. This makes use of the knowledge that in the mixed bed unit subordinate bicarbonate is replaced and this is therefore retained in the treated heating water. The bicarbonate contributes to the buffer effect.
    It is particularly preferred that the mixing bed unit is integrated in the heating circuit in such a way that the heating water flowing through the mixed bed unit has a temperature in the range between 40.degree. C. and 60.degree. In this temperature range, OH- dissolves relatively rapidly from the anion exchanger, which improves the desired functionality of the demineralizer as described above.
    The object of the invention relating to the device for adjusting the pH of the heating water of a heating system by means of a demineralizer to a target pH in the range between 8 and 11 is achieved in that the demineralization device has a main flow line and a bypass line parallel thereto, and the mixing bed unit is arranged in the bypass line. As described above, inline desalination can thus be performed without interrupting the heating operation.
    Particularly preferably, it can be provided that in the bypass line in the flow direction in front of the Mischbetteinheit a filter is arranged. This filter is used to filter out solids from the heating water, which may affect the functionality of the mixed bed.
    Preferably, the device according to the invention may be such that the main flow line and the bypass line are arranged in a structural unit, in particular a housing, and that the mixed bed unit can be exchangeably connected to the bypass line outside the structural unit. This device is easy to handle. When the mixed bed unit is exhausted, it can easily be exchanged for another mixed bed unit.
    The invention will be explained in more detail below with reference to an embodiment shown in the drawings. 1 shows a schematic representation of a heating system with a demineralization device and
    2 shows the Entminteralisierungseinrichtung according to Figure 1 in detail view
    Figure 1 shows a heating system 60 with a buffer memory 63, which is associated with a solar system 61 via a line. About the solar system 61, hot water can be produced that is supplied via the line 62 to the buffer memory 63. Furthermore, a circulation line is connected to the buffer memory 63. In a laxative line, coming from the buffer memory 63, a pump 64 is integrated. This laxative line is connected to a heat exchanger 65. The heat exchanger 65 is part of a heating system, for example a gas or oil thermal. From the heat exchanger 65 is a line 66, which merges into a main flow line 14. Parallel to this main flow line, a bypass line 16 is arranged, in which a mixed bed unit 50 of a demineralization device 10 is integrated. From the mixed bed unit 50 leads a 7/15 7
    Connecting line 18 back to the main flow line 14. Following the main flow line 14 of the water cycle is fed back to the buffer memory 63. As Figure 1 further reveals, a boiler 67 is integrated into the water cycle, which is connected via a line 67.1 to the line 66. Following the boiler 67 is a line 67.2 from, in which a pump 64 is integrated. This line 67.2 opens again in the coming of the buffer memory 63 following the pump 64 line.
    In Figure 2, the demineralizer 10 is shown in detail. As can be seen from this illustration, the demineralization device 10 has a housing which is equipped with rollers 11 and a handle 12 for facilitated transport. In the housing, the main flow line 14 and parallel to the bypass line 16 is arranged. The main flow line 14 and the bypass line 16 open into a feed line 13. Following the feed line 13, a pump 20 is integrated in the bypass line 16. In the flow direction behind the pump 20, a filter 30 is integrated into the bypass line 16. Behind the filter 30, the bypass line 16 is passed by means of a connecting line 17 through the housing of a control unit 40. In the control unit 40, a flow sensor marked D in FIG. 1 is integrated. The control unit 40 has a display with associated controls 41. To the connecting line 17, a connecting line 51 can be connected via a quick coupling. Preferably, the connecting pipe 51 is a flexible hose leading to a head 52 of a mixed bed unit 50. Furthermore, a preferred also flexible connecting line 53 is connected to the head piece 52, which is coupled via a quick coupling to a connecting line 18. The connection line 18 is arranged in the housing of the demineralization device 10. The connecting line 18 and the main flow line 14 lead to a water outlet 15. The demineralization device 10 can be connected by means of the feed line 13 and the water outlet 15 to the heating circuit, as can be seen Figure 1. 8/15 8
    The mixed bed unit 50 is designed as a housing through which water can flow. This enclosure contains a mix of strong base anion exchangers and strong acid cation exchangers. The anion exchanger used can be a styrene resin with OH-activated groups. For example, styrene resins having activated sulfonic acid groups can be used as cation exchangers. The styrene resins are in granular form. The mixing ratio is in the range of 60 to 70% by weight of anion exchanger and 30 to 40% by weight of cation exchanger. The anion exchangers and cation exchangers are mixedly arranged in the housing of the mixed bed unit 50. The mixed bed unit 50 has water guiding structures in the housing by means of which the heating water coming from the connection line 51 can be introduced into the mixed bed 50 via the head piece 52. After flowing through the mixed bed, the heating water then passes through the head piece 52 in the connecting line 53rd
    The operation of demineralizer 10 is as follows:
    Heating water passes from the heating circuit via the feed line 13 into the demineralization device. This heating water flow is split between the main flow line 14 and the bypass line 16. By means of the pump 20, the heating water is conveyed through the bypass line 16 and passes first to the filter 30. Here, solids are filtered out in tap water. For example, magnetite is secreted. Following the filter 30, the heating water flows through the housing of the control unit 40. Here, the volume flow of the heating water is determined by means of the flow meter D. The water then passes via the connecting line 51 to the mixed bed unit 51 and flows through it. In the mixed bed unit 50 minerals are bound from the heating water. At the same time, the anion exchangers OH and the cation exchangers transfer H + into the heating water. Due to the excess of anion exchanger in the mixed bed, an excess of OH is introduced into the heating water compared to the H +. As a result, the pH of the heating water is raised. After the heating water treated in this way has passed through the mixed bed unit 50, it passes through the water outlet 15 back into the heating circuit. The heating water is continuously circulated through the heating circuit, so that the pH is steadily raised at the mixing bed unit 50. If, as in the present embodiment, aluminum parts, for example, an aluminum heat exchanger 65 are integrated into the heating circuit, then the pH should be brought to a target pH in the range between 8.2 and 8.5. If the starting water is present, for example, in the pH range of 7, then the heating water is circulated over the mixed bed unit 50 until it has the desired target pH of 8.2 to 8.5. If the starting water now exists in the pH range> 8.5, then the heating water is first brought to a pH value> 8.5 due to the excess metered addition of OH- in the mixed bed unit 50. The heating water is then circulated over the Mischbetteinheit 50 until the anion exchanger is exhausted and release relatively small amounts of OH- as the cation exchanger H + to the heating water. From this operating point, the heating water is alkalized again and thus the pH value is lowered. The pump 20 is then driven until the desired pH range between 8.2 and 8.5 is reached.
    The pH value of the heating water can be estimated by means of a conductivity sensor M1 for a given hard quality of the water, which is characterized in FIG.
    If in the circulation operation by means of the flow meter D, for example, due to a blocking of the filter 30 or the mixed bed, the falling below a permissible volume flow is detected, the pump 20 is turned off and this signaled via the display unit of the control unit 40. Likewise, the achievement of the target pH value is signaled on the display of the control unit 40 on the basis of a measurement on the conductivity meter M1. The conductivity meter M2 in the connecting line 18 of the bypass line 16 in the flow direction behind the mixing bed unit 50 detects the ionic slippage by the mixing bed unit 50 and can therefore be used to detect the degree of exhaustion of the mixed bed in the mixed bed unit 50. When the mixed bed is exhausted, ions increasingly emerge from the mixed bed increasing the conductivity of the treated heating water. The degree of exhaustion of the mixed bed can also be signaled on the display of the control unit.
    Vienna, 6.2.2014 11/15
    权利要求:
    Claims (14)
    [1]
    Dr. Müllner Dipl.-Ing. Katschinka OG, Patent Attorney Office Weihburggasse 9, Postfach 159, A-1014 WIEN, Austria Phone: C +43 (1) 512 24 81 / Fax: S + 43 (1) 513 76 81 / E-Mail: θ repatent@aon.at Account (PSK): 1480 708 BLZ 60000 BIC: OPSKATWW IEAN: AT19 6000 0000 0148 07081 480 708 16/46085 Perma-trade Wassertechnik GmbH D-71229 Leonberg (DE) Claims: 1. A method for adjusting the pH of the heating water of a Heating system by means of a demineralizer (10) to a target pH in the range between 8 and 10, wherein the heating water is passed through a Mischbetteinheit (50) containing anion and cation exchanger, characterized in that the heating water through the Mischbetteinheit (50 ) is first circulated to bring it to a higher pH, and subsequently that the heating water is circulated through the mixing bed unit (50) such that it is acidified to reach the target pH.
    [2]
    2. The method according to claim 1, characterized in that the Mischbetteinheit (50) has a relation to the cation exchangers higher content of anion exchangers, preferably in the range between 60 wt% and 70 wt% anion exchanger and 30 wt% to 40 wt% cation exchanger.
    [3]
    3. The method according to claim 1 or 2, characterized in that the heating water is transferred to a target pH in the range between 8, 2 to 8.5.
    [4]
    4. The method according to any one of claims 1 to 3, characterized in that the heating water via a main flow line (14) and in parallel via a bypass line (16) is passed, and that the Mischbetteinheit (50) in the bypass line (16) is arranged ,
    [5]
    5. The method according to claim 4, characterized in that the Mischbetteinheit (50) is associated with a pump (20) in the bypass line (16). 12/15 2
    [6]
    6. The method according to any one of claims 1 to 5, characterized in that the Mischbetteinheit (50) is associated with a flow meter (D) with which the over the Mischbetteinheit (50) directed heating water flow is measured.
    [7]
    7. The method according to any one of claims 1 to 6, characterized in that with a flow direction behind the Mischbetteinheit (50) arranged conductivity sensor (M2), the electrical conductivity of the coming from the Mischbetteinheit heating water is determined.
    [8]
    8. The method according to any one of claims 4 to 7, characterized in that the pH of the heating water is determined outside the bypass line, in particular the electrical conductivity of the heating water is measured.
    [9]
    9. The method according to any one of claims 1 to 8, characterized in that the heating water by means of the demineralization device (10) is only partially desalted, wherein the salt content is adjusted such that the heating water upon reaching the target pH, an electrical conductivity in the range between 100 yS / cm and 200 yS / cm.
    [10]
    10. The method according to any one of claims 1 to 9, characterized in that the Mischbetteinheit (50) is integrated in the heating circuit, that by the Mischbetteinheit (50) flowing heating water has a temperature in the range between 40 ° C to 60 ° C.
    [11]
    11. A device for adjusting the pH of the heating water of a heating system by means of a demineralization device (10) to a target pH in the range between 8 and 11, wherein the heating water is passed through a Mischbetteinheit (50) containing anion and cation exchanger, characterized characterized in that the demineralisation device (10) has a main flow line (14) and, parallel thereto, a bypass line (16), and that the mixed bed unit (50) is arranged in the bypass line (16).
    [12]
    12. The device according to claim 11, characterized in that in the bypass line (16) in the flow direction in front of the Mischbetteinheit (50) a filter (30) is arranged.
    [13]
    13. The apparatus of claim 11 or 12, characterized in that the main flow line (14) and the bypass line (16) are arranged in a structural unit, in particular a housing, and that the Mischbetteinheit (50) outside the unit replaceable to the bypass line (17 ) is connectable.
    [14]
    14. Device according to one of claims 11 to 13, characterized by one of claims 1 to 10 Vienna, 6.2.2014 14/15
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE102005036356C5|2005-07-29|2015-09-10|Perma-Trade Wassertechnik Gmbh|Water treatment device for a heating system|
    DE102007009959A1|2007-03-01|2008-09-04|Klaus Seifert|Method for removing especially inorganic deposits in heating or cooling circuits using ion exchange resin in bypass or in main feed|
    DE102008003327A1|2008-01-07|2009-07-09|Perma-Trade Wassertechnik Gmbh|Water treatment device for a heating system|
    DE102009027144A1|2009-06-24|2011-06-22|Judo Wasseraufbereitung GmbH, 71364|Apparatus for treating feed water for a water cycle|
    DE202010004292U1|2010-03-26|2010-07-01|Vws Deutschland Gmbh|Module for the treatment of heating circuit water|
    DE102010029516A1|2010-05-31|2011-12-01|Brita Professional Gmbh & Co. Kg|Apparatus for treating process water|DE102016218227A1|2016-09-22|2018-03-22|Robert Bosch Gmbh|Water treatment module for reducing the conductivity of circulating water|
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    DE102018129862A1|2018-11-27|2020-05-28|Perma-Trade Wassertechnik Gmbh|Method and device for reducing the oxygen content of heating water|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE102013102426.2A|DE102013102426A1|2013-03-12|2013-03-12|Method and device for adjusting the pH value of the heating water of a heating system|
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