Interruption of measured variable analyses in an automatic water softening system when defined operating situations are present

• US 8,668,830 B2
• Filed: 08/13/2009
• Issued: 03/11/2014
• Est. Priority Date: 09/02/2008
• Status: Active Grant

• Current Assignee: Judo Wasseraufbereitung Gmbh (Dopslaff Grundstuecksgesellschaft)
• Original Assignee: Judo Wasseraufbereitung Gmbh (Dopslaff Grundstuecksgesellschaft)
• Inventors: Soecknick, Ralf, Neidhardt, Klaus, Haug, Alexander, Melcher, Siegfried
• Primary Examiner(s): Savage, Matthew O
• Application Number:
  US13/058,503
• Publication Number:
  US 20110139720A1
• Time in Patent Office: 1,671 Days
• Field of Search: 210/96.1, 210/100, 210/101, 210/662, 210/739, 210/746, 210/670, 210/687, 137/5, 700/239, 700/271, 700/285
• US Class Current: 210/662
• CPC Class Codes: B01J 49/85 Controlling or regulating devices therefor
• CPC Class Codes: C02F 1/008 Control or steering systems not provided for elsewhere in subclass C02F
• CPC Class Codes: C02F 1/42 by ion-exchange ion-exchange in general B01J
• CPC Class Codes: C02F 2209/001 Upstream control, i.e. monitoring for predictive control
• CPC Class Codes: C02F 2209/003 Downstream control, i.e. outlet monitoring, e.g. to check the treating agents, such as halogens or ozone, leaving the process
• CPC Class Codes: C02F 2209/05 Conductivity or salinity
• CPC Class Codes: C02F 2209/055 Hardness
• CPC Class Codes: C02F 2209/40 Liquid flow rate
• CPC Class Codes: C02F 2301/043 Treatment of partial or bypass streams

Abstract

A method for operating a water softening system (1) comprising

• • an automatically adjustable blending means for mixing a blended water flow V(t)_blended from a first, softened partial flow V(t)_part1soft and a second untreated water partial flow V(t)_part2raw and comprising
  • an electronic control means (11),
    wherein the control means (11) readjusts the adjustment position of the blending means by means of one or more experimentally determined instantaneous measured values in such a fashion that the water hardness in the blended water flow V(t)_blended is adjusted to a predetermined desired value (SW),
    is characterized in that
    the control means (11) ignores at least one of the one or more instantaneous measured values for readjustment of the adjustment position of the blending means in one or more defined operating situations, and instead uses the respectively last corresponding measured value that was valid prior to occurrence of the defined operating situation, or a standard value for the corresponding measured value, which is stored in the electronic control means (11). The inventive method reduces the wear of the automatically adjustable blending means and improves the reliability of the adjustment of the water hardness of the blended water.

Claims

1. A method for operating a water softening blending system comprising:

mixing a blended water flow V(t)_blended from a first, softened partial flow V(t)_part1soft and a second untreated water partial flow V(t)_part2raw with an automatically adjustable blender; and

readjusting an adjustment position of the blender with an electronic controller using one or more experimentally determined instantaneous measured values in such a fashion that a water hardness in the blended water flow V(t)_blended is adjusted to a predetermined desired value (SW), and

wherein the electronic controller ignores at least one of the one or more instantaneous measured values for readjustment of the adjustment position of the blender in one or more defined operating situations of the water softening blending system, and instead uses a respectively last corresponding measured value that was valid prior to occurrence of the defined operating situation, or a standard value for a corresponding measured value, which is stored in the electronic controller,

wherein the method comprises a sensor in an untreated water area of the water softening blending system for determining an instantaneous untreated water hardness WH_raw^inst and at least two flow meters for direct or indirect determination of instantaneous partial flows V(t)_part1soft^inst and V(t)_part2raw^inst and the electronic controller ignores at least one of the instantaneous measured values WH_raw^inst,V(t)_part1soft^inst and V(t)_part2raw^inst for readjustment of the adjustment position of the blending device in the defined operating situations, and instead uses a respectively last corresponding measured value that was valid prior to occurrence of the defined operating situation or a standard value for a corresponding measured value, which is stored in the electronic controller.

2. The method according to claim 1, wherein the sensor is designed as a conductivity sensor, which determines an instantaneous electrical conductivity L_raw^inst of the untreated water, that the electronic controller determines the instantaneous untreated water hardness WH_raw^inst from the determined instantaneous conductivity L_raw^inst of the untreated water, and wherein the electronic controller furthermore determines an instantaneous desired ratio of the partial flows V(t)_part1soft and V(t)_part2raw from the determined instantaneous untreated water hardness WH_raw^inst by means of which the predetermined desired value (SW) of the water hardness is established in the blended water flow V(t)_blended, and wherein the electronic controller readjusts the adjustment position of the blender to the instantaneous desired ratio according to the determined instantaneous partial flows V(t)_part1soft^inst and V(t)_part2raw^inst.

3. The method according to claim 1 wherein the electronic controller ignores the measured values for the two instantaneous partial flows V(t)_part1soft^inst and V(t)_part2raw^inst only in combination together.

4. The method according to claim 1 wherein the defined operating situations include times when the ratio between the measured values V(t)_part1soft^inst and V(t)_part2raw^inst has changed since the last readjustment of the adjustment position of the blending means by less than a relative flow change value, and wherein the relative flow change value is between 2% and 10%.

5. The method according to claim 1 wherein the defined operating situations include the times of regeneration of a softening device.

6. The method according to claim 1 wherein the defined operating situations include falling below a minimum flow rate and/or exceeding a maximum flow rate at a flow meter.

7. The method according to claim 1 wherein the defined operating situations include times when there is a hardness breakthrough at a water softening system supplying the softened partial flow V(t)_part1soft.

8. The method according to claim 1 wherein the defined operating situations include times when a leakage is detected at a water softening system supplying the softened partial flow V(t)_part1soft, the water softening blending system or any downstream water installation.

9. The method according to claim 1 wherein in at least part of the defined operating situations, the electronic controller completely suspends readjustment of the adjustment position of the blender such that the blended water flow is mixed with the last adjustment position of the blender, which was set prior to occurrence of the defined operating situation.

10. The method according to claim 1 wherein the water softening blending system comprises a conductivity sensor in an untreated water area for determining the instantaneous conductivity of the untreated water L_raw^inst, and that the defined operating situations include times when the instantaneous measured value L_raw^inst has changed by less than a predefined conductivity difference value since the last readjustment of the adjustment position of the blending means, wherein the conductivity difference value is between 5μ

S/cm and 50μ

S/cm.

11. The method according to claim 1 wherein the defined operating situations include times when at least a minimum amount of water has not been continuously flowing through the water softening blending system directly prior to an intended evaluation of one or more of the instantaneous measured values.

12. The method according to claim 1 wherein the defined operating situations include times when water has not been continuously flowing through the water softening blending system for at least a minimum duration directly prior to an intended evaluation of one or more of the instantaneous measured values.

13. The method according to claim 1 wherein the water softening blending system further comprises a supply container for providing regenerant solution and apparatus for automatic performance of regeneration of a softening device, and the electronic controller automatically triggers regeneration of the softening device in dependence on soft water withdrawals performed since a the last regeneration of the softening device.

14. The method according to claim 13, wherein the electronic controller detects a residual capacity of the softening device in dependence on the soft water withdrawals performed since a last triggered regeneration, and on one or more associated determined untreated water hardnesses, and upon depletion thereof, automatically triggers regeneration of the softening device .

15. The method according to claim 14 wherein the water softening blending system comprises a conductivity sensor in the untreated water area, and that an overall hardness I of the untreated water, which hardness is used to control the regeneration process of the softening device is derived from the measured conductivity L_raw by means of a first calibration characteristic (F1), and an overall hardness II of the untreated water, which hardness is used to control the blending means, is derived from the measured conductivity L_raw using a second calibration characteristic (F2).

16. The method according to claim 15, wherein the overall hardness I derived from the first calibration characteristic (F1) is greater, at least in sections, than the overall hardness II derived from the second calibration characteristic (F2).

17. The method according to claim 13 wherein the electronic controller ignores at least one of the one or more instantaneous measured values also for automatic triggering of regeneration of a softening system in one or more defined operating situations, and instead uses a respectively last corresponding measured value that was valid prior to occurrence of the operating situation, or a standard value for a corresponding measured value, which is stored in the electronic controller.

18. A method for operating a water softening blending system comprising:

mixing a blended water flow V(t)_blended from a first, softened partial flow V(t)_part1soft and a second untreated water partial flow V(t)_part2raw with an automatically adjustable blender; and

readjusting an adjustment position of the blender with an electronic controller using one or more experimentally determined instantaneous measured values in such a fashion that a water hardness in the blended water flow V(t)_blended is adjusted to a predetermined desired value (SW), and

wherein the electronic controller ignores at least one of the one or more instantaneous measured values for readjustment of the adjustment position of the blender in one or more defined operating situations of the water softening blending system, and instead uses a respectively last corresponding measured value that was valid prior to occurrence of the defined operating situation, or a standard value for a corresponding measured value, which is stored in the electronic controller,

wherein the defined operating situations include times when an experimentally determined instantaneous water hardness, an instantaneous untreated water hardness WH_raw^inst or an instantaneous blended water hardness WH_blended^inst is outside of a predetermined value interval.

19. The method according to claim 18 wherein the defined operating situations include times when the experimentally determined instantaneous water hardness, the instantaneous untreated water hardness WH_raw^inst or the instantaneous blended water hardness WH_blended^inst has changed by less than a predefined hardness difference value since the last readjustment of the adjustment position of the blending means, in particular, wherein the hardness difference value is between 0.2°

dH and 2.0°

dH.

20. The method according to claim 18, wherein the predetermined value interval ranges from 2°

dH to 50°

dH.

21. The method according to claim 18, wherein the water softening blending system comprises a sensor in a blended water area of the water softening blending system for determining the instantaneous blended water hardness WH_blended^inst, and that the electronic controller ignores at least the instantaneous measured value WH_blended^inst for readjustment of the adjustment position of the blender in the defined operating situations, and instead uses the last defined blended water hardness that was valid prior to occurrence of the defined operating situation or a standard value for the blended water hardness, which is stored in the electronic controller.