CN110998307B - Management system of water treatment equipment - Google Patents
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 239000013043 chemical agent Substances 0.000 claims 1
- 238000012937 correction Methods 0.000 abstract description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 16
- 229910021529 ammonia Inorganic materials 0.000 description 8
- 238000002347 injection Methods 0.000 description 6
- 239000007924 injection Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 239000003814 drug Substances 0.000 description 4
- 150000001412 amines Chemical class 0.000 description 3
- 229940079593 drug Drugs 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- PAFZNILMFXTMIY-UHFFFAOYSA-N cyclohexylamine Chemical compound NC1CCCCC1 PAFZNILMFXTMIY-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001139 pH measurement Methods 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- FAXDZWQIWUSWJH-UHFFFAOYSA-N 3-methoxypropan-1-amine Chemical compound COCCCN FAXDZWQIWUSWJH-UHFFFAOYSA-N 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000007405 data analysis Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000003002 pH adjusting agent Substances 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
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- G01N27/00—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D11/00—Feed-water supply not provided for in other main groups
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- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
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- G01N27/28—Electrolytic cell components
- G01N27/30—Electrodes, e.g. test electrodes; Half-cells
- G01N27/302—Electrodes, e.g. test electrodes; Half-cells pH sensitive, e.g. quinhydron, antimony or hydrogen electrodes
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
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Abstract
Description
技术领域technical field
本发明涉及锅炉的供水系统等的水处理设备的管理系统。更详细来说,本发明涉及利用预先设定的任意规定温度条件下的电导率与pH的相关关系来进行管理的水处理设备的管理系统。The present invention relates to a management system of water treatment equipment such as a boiler water supply system. More specifically, the present invention relates to a management system for water treatment equipment that manages using a preset correlation between conductivity and pH under arbitrary predetermined temperature conditions.
背景技术Background technique
专利文献1公开了设备管理系统的管理中心定期收集水处理设备的设备运作信息,管理运作状态。专利文献1公开了一边参照蓄积于数据库的参照信息,一边依据设备运作信息、被处理水的分析结果来详细分析水处理设备的运作状态。专利文献1公开了制作与有助于运作水处理设备的运转条件相关的建议信息、维护信息等,并提示于供水处理设备侧。
确认能保证现场仪器的正确程度对于提升水处理效果而言是重要课题。在发电锅炉的水处理设备的情况下,pH是重要的管理项目,其适用范围也记载于JIS B8223:2015。在专利文献2中记载了锅炉的供水管理装置,其使用多个pH计来相互实施校正,或观察由电导率计所换算的pH值的相关。专利文献2的管理装置需要准备多个pH计,并比较它们的值。专利文献2的管理装置的问题在于,因样本温度而使pH值本身变动,从而使pH值产生漂移。为使现场的样本水温始终保持恒定的状态而实施冷却水量的调整等是非常困难的。It is an important issue to confirm the accuracy of on-site instruments to improve the water treatment effect. In the case of water treatment equipment for power generation boilers, pH is an important management item, and its scope of application is also described in JIS B8223:2015.
现有技术文献prior art literature
专利文献:Patent documents:
专利文献1:日本专利第3624941号公报;Patent Document 1: Japanese Patent No. 3624941;
专利文献2:日本特开2002-349804号公报。Patent Document 2: Japanese Unexamined Patent Publication No. 2002-349804.
发明内容Contents of the invention
本发明的目的在于提供一种水处理设备的管理系统,其能防止在pH计的偏移、校正的偏差未被消除的状态下进行水处理管理,能进行稳定的水处理管理。It is an object of the present invention to provide a management system for water treatment facilities that can prevent water treatment management in a state where pH meter deviation and calibration deviation are not eliminated, and can perform stable water treatment management.
第1发明的水处理设备的管理系统是具有pH计及电导率计的水处理设备的管理系统,其特征在于,具备:第1存储机构,存储电导率与pH的相关关系;第2存储机构,存储pH与水温的相关关系;以及管理机构,依据由电导率计测定的电导率与存储于所述第1存储机构的所述相关关系,求出理论pH值,依据存储于所述第2存储机构的相关关系与水温,将前述pH计的检测pH值换算成规定温度的pH值,在理论pH值与换算pH值偏离规定值以上的情况下,发出促使pH计校正的信号。The water treatment facility management system of the first invention is a water treatment facility management system having a pH meter and a conductivity meter, and is characterized in that it includes: a first storage mechanism for storing the correlation between conductivity and pH; a second storage mechanism , storing the correlation between pH and water temperature; and the management agency, based on the electrical conductivity measured by the conductivity meter and the correlation stored in the first storage mechanism, to obtain a theoretical pH value, based on the correlation stored in the second The correlation between the storage mechanism and the water temperature converts the pH value detected by the pH meter into a pH value at a specified temperature, and sends a signal to urge the pH meter to calibrate if the theoretical pH value and the converted pH value deviate from the specified value or more.
第2发明的水处理设备的管理系统是具有电导率计的水处理设备的管理系统,其特征在于,具备:存储机构,存储规定温度条件下的电导率与pH的相关关系;以及求出pH值的机构,依据由电导率计测定的电导率与存储于所述存储机构的所述相关关系,来求出pH值。The water treatment facility management system of the second invention is a water treatment facility management system having a conductivity meter, characterized in that it includes: a storage mechanism for storing the correlation between conductivity and pH under predetermined temperature conditions; and calculating the pH The means for obtaining the pH value is based on the correlation between the conductivity measured by the conductivity meter and the correlation stored in the storage means.
在本发明的一方式中,前述规定温度为25℃。In one aspect of this invention, the said predetermined temperature is 25 degreeC.
在本发明的一方式中,前述水处理设备以锅炉供水为对象。In 1 aspect of this invention, the said water treatment facility targets boiler water supply.
在本发明的一方式中,前述管理机构发送包含药剂注入量调整或排放量调整的建议信号。In one aspect of the present invention, the management unit transmits a recommendation signal including adjustment of injection amount of medicine or adjustment of discharge amount.
依据本发明,换算成规定温度条件下的pH的pH与根据电导率所求出的pH值偏离规定值以上时,进行促使校正的显示,或根据电导率来推定pH,由此,防止依据误差大的pH测定值进行的水处理管理,实现稳定的水处理管理。According to the present invention, when the pH converted to the pH under the predetermined temperature condition deviates from the pH value obtained from the conductivity by more than the specified value, a display prompting correction is performed, or the pH is estimated from the conductivity, thereby preventing errors based on Water treatment management with a large pH measurement value realizes stable water treatment management.
附图说明Description of drawings
图1是表示实施方式的框图。FIG. 1 is a block diagram showing an embodiment.
图2是表示pH与电导率的关系的图表。Fig. 2 is a graph showing the relationship between pH and conductivity.
图3是表示控制例的示意图表。FIG. 3 is a schematic diagram showing a control example.
图4是表示pH与温度的关系的图表。Fig. 4 is a graph showing the relationship between pH and temperature.
具体实施方式Detailed ways
以下,参照附图,对实施方式进行说明。图1表示本发明的水处理设备的管理系统的一例。水处理设备(例如发电锅炉用水处理设备)1中,通过药剂注入装置2,添加注入氨、中和性胺、联氨等碱性的药剂。Embodiments will be described below with reference to the drawings. FIG. 1 shows an example of the management system of the water treatment facility of the present invention. In water treatment equipment (for example, water treatment equipment for power generation boilers) 1 , alkaline chemicals such as ammonia, neutral amines, and hydrazine are added and injected through a
作为管理水处理设备1的水质的现场仪器3的一部分,设置有pH计、电导率计、水温计等,该等数据被传送至判定装置(例如PLC)4。在判定装置4设置有判定部4a、显示部4b及发送部4c,将由pH计测定的pH值换算成规定温度的pH值,确认该换算pH值未与根据电导率所求出的理论pH值偏离,同时,将数据传送至管理中心5。在管理中心5中蓄积该等信息,在与先前不同时,则与预先登记于数据解析部的现象进行比较,使建议显示部6显示药液注入量的调整、锅炉水排放量的调整等的建议。作为建议显示部6,使用个人计算机、便携式终端等。A pH meter, a conductivity meter, a water temperature meter, and the like are provided as part of the
判定装置4的判定部4a例如以存储机构存储后述图4所示的pH-温度关系线,在将由pH计测定的pH值换算成规定温度(理想为25℃)的pH值而得到的换算pH值,与根据电导率计的电导率所求出的理论pH值偏离时,使显示部4b显示促使校正的建议显示,并且也将相同内容传送至管理中心5。由此,经由管理中心5,也于建议显示部6进行相同的建议显示。该显示可以邮件发送,也可以显示于特定的WEB页面,对该WEB页面进行访问从而得知。The judging unit 4a of the
在现场的pH计因劣化、破损等而使pH测定值的误差(与依据电导率计的电导率所运算出的理论pH值偏离)变大时,可以设为以判定装置4的显示部4b显示根据电导率换算的理论pH值,并且传送至管理中心5的构造。When the pH meter on site has a large error in the measured pH value (deviation from the theoretical pH value calculated based on the conductivity of the conductivity meter) due to deterioration, damage, etc., the display unit 4b of the
pH值与电导率的相关关系线可以是20℃、30℃等的温度条件下的相关关系线,但在考虑锅炉的水管理时,优选例如以能够依据JIS B8223(2015)的方式设为25℃的相关关系线。The correlation line between the pH value and the conductivity may be a correlation line under temperature conditions such as 20°C and 30°C, but when considering boiler water management, it is preferable to set it to 25 so that it can comply with JIS B8223 (2015), for example. ℃ correlation line.
通过电导率计所测定的电导率相比于pH值,受温度(水温)的影响较小,所以,可以不进行温度换算,但为了更正确地进行测定,优选以电极附属的温度换算功能等进行修正。The conductivity measured by the conductivity meter is less affected by temperature (water temperature) than the pH value, so temperature conversion may not be performed, but in order to measure more accurately, it is preferable to use the temperature conversion function attached to the electrode, etc. Make corrections.
在本实施方式中,如上所述,将pH计的测定pH值换算成规定温度的pH值,在该换算pH值与根据电导率所求出的理论pH值偏离规定值以上时进行校正指示显示。该偏离的规定值优选为从0.1~0.5之间选择的值,例如0.3,优选设为0.2左右。In this embodiment, as described above, the measured pH value of the pH meter is converted into a pH value at a predetermined temperature, and when the converted pH value deviates from the theoretical pH value obtained from the conductivity by a predetermined value or more, a correction instruction is displayed. . The predetermined value of the deviation is preferably a value selected from 0.1 to 0.5, for example, 0.3, preferably about 0.2.
在建议显示中,不仅是依据pH计、电导率计的显示,还可以包含使用更微量的测定仪器得到的结果。In the suggested display, not only the display based on the pH meter and the conductivity meter, but also the results obtained by using a more minute measuring instrument can be included.
用于促使pH计校正的建议显示的信号,例如可以是与每隔1小时传送的定期性数据一起发送的信号,但优选在pH测定值与理论值偏离规定值以上时无迟滞地发送。为使在pH计的校正中不发生促使校正的建议,可以设置校正中按键,或设置在规定期间以内(例如30分钟之间)不发出促使校正的信号的构造等。The signal for displaying a suggestion for pH meter calibration may be, for example, a signal transmitted with periodic data transmitted every hour, but is preferably transmitted without delay when the measured pH value deviates from the theoretical value by a predetermined value or more. In order to prevent a suggestion to prompt calibration during calibration of the pH meter, a calibration button may be provided, or a configuration may be provided so that a signal to prompt calibration is not issued within a predetermined period (for example, within 30 minutes).
实施例Example
[测定例1][Measurement Example 1]
作为锅炉供水的pH调整剂,使用氨、各种胺。由此,测定以各种浓度添加了氨、3-甲氧基丙胺或环己胺的锅炉供水在25℃条件下的pH与电导率。在图2中示出两者的关系(相关关系线)。如图2所示,对应于各种pH调整剂,电导率的对数值与pH为直线关系。所以,在由pH计所致的pH测定值的漂移(在实施例1后述)、由温度所致的误差(在实施例2后述)较大时,通过依据电导率来修正pH计的测定值,能够消除或降低误差。Ammonia and various amines are used as pH regulators for boiler feed water. Thus, the pH and electrical conductivity of boiler feed water to which ammonia, 3-methoxypropylamine, or cyclohexylamine was added at various concentrations were measured at 25°C. The relationship between the two is shown in FIG. 2 (correlation line). As shown in Figure 2, corresponding to various pH regulators, the logarithmic value of conductivity has a linear relationship with pH. Therefore, when the drift of the pH measurement value caused by the pH meter (described later in Example 1) and the error caused by temperature (described later in Example 2) are large, the pH meter is corrected based on the conductivity. The measured value can eliminate or reduce the error.
图2中示出了仅添加1种各pH调整剂至锅炉供水时的相关关系线,但是,组合多种胺、氨来添加时也同样地预先求出相关关系线,依据该相关关系线来求出依据电导率的理论pH值。Fig. 2 shows the correlation line when only one of each pH adjuster is added to the boiler feed water. However, when adding multiple amines and ammonia in combination, the correlation line is similarly obtained in advance, and the correlation line is calculated based on the correlation line Find the theoretical pH value in terms of conductivity.
[比较例1、实施例1][Comparative Example 1, Example 1]
在图3中示出将氨用于锅炉供水的pH调整中的锅炉的探究结果。FIG. 3 shows the results of investigations on boilers using ammonia for pH adjustment of boiler feed water.
在该比较例1及实施例1中所用的pH计具有pH测定值往负方漂移的特性。The pH meters used in Comparative Example 1 and Example 1 have a characteristic that the measured pH value drifts to the negative side.
在图3的左半侧示出比较例1的结果。在比较例1中,如先前一样每个月校正1次pH计,但未实施温度换算。在该比较例1中,未发现pH往负方向漂移,而增加氨的添加量,因此外观上pH(pH计测定值)以恒定值推移,但是,实际上系统内的氨浓度变高,担忧冷凝器中的氨腐蚀。The results of Comparative Example 1 are shown on the left half of FIG. 3 . In Comparative Example 1, the pH meter was calibrated once a month as before, but the temperature conversion was not implemented. In this Comparative Example 1, the pH was not found to drift in the negative direction, but the amount of ammonia added was increased, so the pH (measured value of the pH meter) appeared to change at a constant value, but in fact, the ammonia concentration in the system became high, and there was concern. Ammonia corrosion in condenser.
在图3的右半侧示出实施例1的结果。如图所示,利用本发明方法时,以根据电导率换算的25℃的pH进行管理,因此在经过两个月的期间,实际的pH保持为恒定,持续进行适当的药剂注入管理。The results of Example 1 are shown in the right half of FIG. 3 . As shown in the figure, when the method of the present invention is used, the pH is managed at 25°C converted from the conductivity, so the actual pH is kept constant for two months, and appropriate drug injection management is continued.
根据以上内容,确认了依据预先测定的pH与电导率的相关关系线,由电导率测定值推定pH值的方法的有用性。Based on the above, the usefulness of the method of estimating the pH value from the measured value of the conductivity based on the correlation line between the pH and the conductivity measured in advance was confirmed.
[实施例2][Example 2]
使锅炉供水的温度在18~35℃的范围变化,测定pH值。将结果示于图4。如图4所示,在温度与pH之间存在直线关系。所以,显而易见的是,即使是在25℃以外的温度测定的pH值,也能够通过使用换算式来换算成25℃的pH值。The temperature of boiler feed water was changed in the range of 18 to 35°C, and the pH value was measured. The results are shown in Fig. 4 . As shown in Figure 4, there is a linear relationship between temperature and pH. Therefore, it is obvious that even the pH value measured at a temperature other than 25°C can be converted into a pH value at 25°C by using a conversion formula.
通过依据换算成25℃的pH值来进行药剂注入控制,能进行更适当的药品注入量的调整。需要说明的是,图4的换算式如下。By performing drug injection control based on the pH value converted to 25°C, more appropriate adjustment of the drug injection amount can be performed. It should be noted that the conversion formula in FIG. 4 is as follows.
pH[at25℃]=pH[atM℃]+(M-25)×0.035pH[at25°C]=pH[atM°C]+(M-25)×0.035
已使用特定方式来详细说明本发明,但是,本领域技术人员可知在不脱离本发明的意图与范围的情况下可进行各种变更。Although this invention was demonstrated in detail using the specific form, it is clear for those skilled in the art that various changes can be made without deviating from the intent and range of this invention.
本申请基于2017年9月7日申请的日本专利申请2017-172246,通过引用来援用其全部内容。This application is based on Japanese Patent Application No. 2017-172246 filed on September 7, 2017, the entire contents of which are incorporated herein by reference.
附图符号说明Description of reference symbols
1:水处理设备;1: Water treatment equipment;
4:测定装置;4: Measuring device;
5:管理中心;5: Management Center;
6:建议显示部。6: Recommended display section.
Claims (3)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2017172246A JP6471785B1 (en) | 2017-09-07 | 2017-09-07 | Management system for water treatment facilities for power generation boilers |
JP2017-172246 | 2017-09-07 | ||
PCT/JP2018/028581 WO2019049556A1 (en) | 2017-09-07 | 2018-07-31 | Management system of water treatment facility |
Publications (2)
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CN110998307A CN110998307A (en) | 2020-04-10 |
CN110998307B true CN110998307B (en) | 2023-01-20 |
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CN201880053238.7A Active CN110998307B (en) | 2017-09-07 | 2018-07-31 | Management system of water treatment equipment |
Country Status (5)
Country | Link |
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JP (1) | JP6471785B1 (en) |
KR (1) | KR102603844B1 (en) |
CN (1) | CN110998307B (en) |
TW (1) | TW201913003A (en) |
WO (1) | WO2019049556A1 (en) |
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CN111909033A (en) * | 2020-08-17 | 2020-11-10 | 日照金禾博源生化有限公司 | Method for reducing yield of weak acid in citric acid extraction process |
CN112946027A (en) * | 2021-03-11 | 2021-06-11 | 烟台方心水处理设备有限公司 | pH on-line detection method for super-alkaline electrolyzed water |
CN115771940A (en) * | 2022-12-16 | 2023-03-10 | 国网湖南省电力有限公司 | Intelligent adjusting device for pH value of inner cooling water and application method thereof |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2002349804A (en) * | 2001-05-29 | 2002-12-04 | Mitsubishi Heavy Ind Ltd | Water supply management device for boiler, water supply control method for boiler and water supply management method for boiler |
CN101045572A (en) * | 2006-03-31 | 2007-10-03 | 栗田工业株式会社 | Treatment method and device for water system of purified water boiler |
JP2008190969A (en) * | 2007-02-02 | 2008-08-21 | Dkk Toa Corp | Measuring apparatus and data table setting method |
JP2009243972A (en) * | 2008-03-28 | 2009-10-22 | Mitsubishi Heavy Ind Ltd | Water quality monitor for turbine installation and method |
JP2011156529A (en) * | 2009-10-30 | 2011-08-18 | Mitsuyoshi Yamazaki | Flocculant injection rate determination device and flocculant injection rate control system |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
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JP3624941B2 (en) | 2000-03-17 | 2005-03-02 | 栗田工業株式会社 | Equipment management system |
JP4873791B2 (en) * | 2001-05-21 | 2012-02-08 | 株式会社トウスイ | Electrode scale component precipitation suppression device |
JP2008196862A (en) * | 2007-02-08 | 2008-08-28 | Toshiba Corp | System for detecting state of aggregation |
JP2010230570A (en) * | 2009-03-27 | 2010-10-14 | Sysmex Corp | Reagent preparing apparatus and sample analyzer |
CN102323316B (en) * | 2011-08-16 | 2013-10-30 | 浙江大学 | High-temperature high-pressure calibration device and calibration method of pH electrode |
-
2017
- 2017-09-07 JP JP2017172246A patent/JP6471785B1/en active Active
-
2018
- 2018-07-31 KR KR1020207004355A patent/KR102603844B1/en active Active
- 2018-07-31 WO PCT/JP2018/028581 patent/WO2019049556A1/en active Application Filing
- 2018-07-31 CN CN201880053238.7A patent/CN110998307B/en active Active
- 2018-09-06 TW TW107131310A patent/TW201913003A/en unknown
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002349804A (en) * | 2001-05-29 | 2002-12-04 | Mitsubishi Heavy Ind Ltd | Water supply management device for boiler, water supply control method for boiler and water supply management method for boiler |
CN101045572A (en) * | 2006-03-31 | 2007-10-03 | 栗田工业株式会社 | Treatment method and device for water system of purified water boiler |
JP2008190969A (en) * | 2007-02-02 | 2008-08-21 | Dkk Toa Corp | Measuring apparatus and data table setting method |
JP2009243972A (en) * | 2008-03-28 | 2009-10-22 | Mitsubishi Heavy Ind Ltd | Water quality monitor for turbine installation and method |
JP2011156529A (en) * | 2009-10-30 | 2011-08-18 | Mitsuyoshi Yamazaki | Flocculant injection rate determination device and flocculant injection rate control system |
Also Published As
Publication number | Publication date |
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CN110998307A (en) | 2020-04-10 |
JP2019045455A (en) | 2019-03-22 |
WO2019049556A1 (en) | 2019-03-14 |
TW201913003A (en) | 2019-04-01 |
KR102603844B1 (en) | 2023-11-17 |
KR20200050951A (en) | 2020-05-12 |
JP6471785B1 (en) | 2019-02-20 |
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