9000 PLUS - Rohrback Cosasco Systems
Contents
1. s 15 APPENDIXB 22 APPENDIX eT 25 ii 9000 Plus Reference Manual Figures and Drawings Figure Figure 1 1 Figure 3 1 Figure 3 2 Figure 4 1 Figure 4 2 Table 5 1 Figure A 1 Figure A 2 Figure A 3 Figure A 4 Figure B 1 Figure B 2 Figure B 3 Page General View of 9000 Plus 1 Probe Orientation Relative to enne nnne nens 5 Probe Orientation at a Tee Fitting 6 Front Panel of 9000 7 Battery Compartment iii 8 Corrater Multiplier Factors isa 12 Equivalent Circuit of LPR Probe sis 16 Typical LPR Current vs Time Decay Curve sse 17 Operating Range of LPR Instruments Corrosion Rate vs Solution Conductivity 18 Rohrback Cosasco 3 Electrode Probe Configuration 19 Conductivity Correction Factor US CM ss 22 Conductivity Correction Factor mmpy 5 23 Conductivity Correction Factor S cm 24 Chapter 1 Introduction The 9000 Plus CORRATER Instrument is a hand held corrosion monitor for process cooling or potable water systems This instrument is designed to improve facility operations by enabling the user to directly measure general corrosion rate and qualitatively determine pitting tendency using the imbalance measurement Like its predecessor the 9000 the 902. 3 2 cct oii coin E Eoo Lec au 7 GENERA 0 TEE 7 CONEIGURATIONE ERA IC 8 RES me 9 INITIAL START UP PARAMETER 157 04 4 1 esed dads sana ss dass nnana 9 INTERPRETATION OPERATING PARAMETERS AND READING 10 CHAPTER 5 11 INTRODUCTION 15 1c oou RO ul ee 11 INSTRUMENT AND PROBE CABLE 5 0000000 0 asas 11 PROBE ege eet eaa adda dada 11 PROBE CLEANING AND ELECTRODE REPLACEMENT 11 ELECTRODE PRETREATMENT 25 25 aas eue cec De eu out cep ae De 0 13 CORRELATION WITH ELECTRODES AS 13 eni e nde ent eite etched 15 THEORY OF OPERATION OF CORRATER
3. by equation 1 AE ba be 1 meas 2 303 corr ba b where ba Anodic Tafel Slope b Cathodic Tafel Slope Since the Tafel coefficients are more or less constant for a given metal fluid combination imeas 18 proportional to igor which is proportional to the corrosion rate Equation 1 and the entire LPR technique are only valid when the polarizing potential difference is very low typically up to 20 mV In this region the curves are linear hence the term LPR Inspection of Equation 1 shows that the result is a resistance the Polarization Resistance Rp While strictly speaking there are both anodic and cathodic R values which can differ they are usually assumed to be equal The resistance to current flow between anode and cathode on the LPR probe is the sum of both polarization resistance values and the resistance of the solution between the electrodes lt as shown in Equation 2 E imeas QR Rs 2 where Rs Resistance of the solution between the two electrodes From Equations 1 and 2 obtaining results from the LPR technique would seem to require only instantaneous readings of resistance In practice however the determination of polarization resistance is complicated by a capacitance effect at the metal fluid interface double layer capacitance Ca Figure A 1 is an equivalent electrical circuit of the corrosion cell formed by the measuring electrodes and the fluid showing the importance of
4. operation of the instrument Instrument and Probe Cable Test The instrument is shipped from the factory with a test probe RCS part number 011000 5 The test probe will simulate a corrosion rate of 5 1 at a multiplier of 1 0 If acceptable readings are performed on test probes then problems are likely to be caused by the process itself or the probe in service A fouling problem for example can bridge the electrodes and yield readings outside the normal measurement range of the instrument NOTE Be sure to set the multiplier parameter to mild steel when measuring test probes and to return it to its previous setting when completed Probe Replacement Probe replacement is not required except due to damage or deterioration Replace the probe if there is physical damage or a low resistance less than 1 Meg Ohm between the electrodes when disconnected from the electronics Probe Cleaning and Electrode Replacement As supplied from the factory CORRATER electrodes have grit blasted surfaces and require no further cleaning before they are used Probes should be checked at intervals particularly for conductive debris shorting out the electrodes which may be indicated by a very high corrosion rate reading They should be cleaned and polished to a dull shine with an emery cloth After cleaning the electrodes should be thoroughly degreased in a suitable solvent and handled with a clean cloth or paper towel to prevent contamination The i
5. the years to minimize the impact of solution resistance on LPR measurements The most common techniques involved the use of a three electrode probe The effectiveness of the reference electrode in reducing the effect of solution resistance has been shown to be dependent upon the proximity of the reference electrode to the measurement electrode Rohrback Cosasco three electrode probes utilize a closely spaced electrode AUXILIARY TEST REFERENCE Figure 4 Rohrback Cosasco 3 Electrode Probe Configuration A better way to deal with this problem however is to directly measure and compensate for the solution resistance Rohrback Cosasco has exclusive patent rights to the Solution Resistance Compensation SRC technique incorporated in most of the CORRATER range of instruments In this method a high frequency A C voltage signal is applied between the electrodes short circuiting Ry through the double layer capacitance thereby directly measuring the solution resistance The state of the art patented SRC technology also eliminates the need for a third electrode even in low conductivity solutions Consequently Rohrback Cosasco Systems two electrode probes have become the standard RCS offering with the three electrode probe available on special order only The above points are clearly indicated in ASTM Standard Guide G96 which quotes 3 2 8 Two electrode probes and three electrode probes with the reference electrode equidistant from t
6. to promote pitting one electrode will exhibit a more positive corrosion potential Eco than the other The polarity of the open circuit potential difference will indicate which electrode has the greater pitting tendency That electrode will be the more negative of the two If these electrodes are electrically connected through a zero resistance ammeter ZRA the measured short circuit current is a measure of the pitting tendency of the electrode material in the aqueous environment This is the measurement technique that it is utilized in CORRATER 21 instruments to provide qualitative measure of pitting tendency In CORRATER instruments the imbalance or pitting units are each 2 5 uA which corresponds to a current density of 0 5 uA cm the CORRATER electrode surface area is 5 cm The scale factor above was established from empirical data so that the relative magnitudes of corrosion rates and imbalance readings could be compared At this scale factor the dominant corrosion mechanism is the one which exhibits the greater magnitude i e corrosion rate gt imbalance indicates more general corrosion and imbalance gt corrosion rate indicates more pitting activity 22 9000 Plus Reference Manual Appendix B Corrosion Rate Multiplication Factor Conductivity Correction Factor E B E El E E LET
7. water applications conductivity of the solution is high and solution resistance is low compared to the polarization resistance so ime is an accurate measure of polarization resistance and therefore corrosion rate A serious problem develops however when the solution resistance increases or the polarization resistance decreases enough to make the solution resistance a significant portion of the total resistance to current flow between the electrodes In these cases the accuracy of the LPR measurement is affected This situation tends to occur at high corrosion rates low polarization resistance and in solutions with low conductivity high solution resistance and is manifested by the indicated measured corrosion rate being lower than the actual corrosion rate The graph in Figure A 3 shows the effect of this limitation on the recommended operating range of LPR instruments 18 9000 Plus Reference Manual Operating Region Typical Corrosion Rate of Carbon Steel 0 1 f 0 1 1 10 100 1000 10k 100k Conductivity or pmhos cm Normal operating range with direct reading Operating range with conductivity correction applied m e ax Operating range with closed spaced three electrode probe Operating range with 2 electrode and S R C eee Extended operating range with Model 9020E 9020 Figure A 3 Operating Range of LPR Instruments Corrosion Rate vs Solution Conductivity Several techniques have been used over
8. 00 Plus has an easy to use operator interface plus an onboard storage of the last measurement and a menu to adjust for various electrode sizes and metallurgy Figure 1 1 General View of 9000 Plus Unit The 9000 Plus uses the linear polarization resistance technique Like all LPR instruments corrosion rate is determined by measuring the current from a small applied potential difference between two measurement electrodes of the alloy being monitored The 9000 Plus is compatible with all two or three electrode probes already in use discussion of the LPR method of corrosion rate measurement is presented in Appendix A of this manual The 9000 Plus is designed for the convenience of the user The 9000 Plus also monitors a form of Electrochemical Current Noise ECN between the electrodes called imbalance or pitting 2 9000 Plus Reference Manual tendency This is a qualitative and very useful indication of instability in the material surface consistent with pitting or localized corrosion The operator only needs to perform an initial setup to set the engineering units for corrosion rate and set the probe multiplier to the size and or alloy of the electrodes as appropriate Initial setup is performed via fr
9. 9000 PLUS INSTRUMENT Reference Manual Rohrback Cosasco Systems Inc Tel 1 562 949 0123 11841 East Smith Avenue Fax 1 562 949 3065 Santa Fe Springs CA 90670 E mail sales rohrbackcosasco com Web Site www rohrbackcosasco com P N 710750 Manual Rev C A 9000 PLUS Microcor Corrdata Corrosometer Corrater amp Corrotemp and Aquamate are trademarks of Rohrback Cosasco Systems 1991 2007 Rohrback Cosasco Systems Inc rights reserved Windows is a trademark of Microsoft Corporation No part of this manual may be reproduced or transmitted in any form or by any means electronic or mechanical including photocopying and recording for any purpose without the express written permission of Rohrback Cosasco Systems Inc Table of Contents CHAPTER 1 22 1 CHAPTER 2 6 252505 rey Ya vo 3 OPERATIONAL 22520 6 ndo ater Rd M re en 622 3 CHAPTER CORRATER PROBE INSTALLATION rn nnne nnn 5 e Tre n m EAM c Lt ORE a ES a nr 6 CHAPTER 4
10. Rs and double layer capacitance effects 16 9000 Plus Reference Manual Test Auxiliary Electrode Electrode Reference Electrode where used Figure 1 Equivalent Circuit of LPR Probe The effect of the double layer capacitance is to require the direct current flow to initially charge up the capacitors resulting in a decaying exponential current flow curve vs time after application of the polarizing potential difference A typical LPR current vs time curve is shown in Figure A 2 Each metal fluid interface has its own characteristic capacitance which in turn determines the amount of time required to obtain valid measurements of ir and corrosion rate The actual time required can vary from a few seconds up to 20 minutes depending upon the metal process combination being measured Choosing too short a polarization time can result in current readings much higher than the true ico thus causing measured corrosion rate to be lower than actual sometimes by a significant amount Resultant Current Profile Applied Potential Step Typically 10 mV Current Asymtote y lt 5 O gt 0 c 9 5 Qj D 4 gt e Time minutes Figure A 2 Typical LPR Current vs Time Decay Curve Solution resistance Rs can have a significant effect on accuracy if it is relatively high compared to the polarization resistance In most industrial
11. T Se ate 0 0 005 0 01 0 015 0 02 0 025 0 03 Corrosion Rate Reading Conductivity Slem 0 0 35 Figure B 1 Conductivity Correction Factor uS cm Conductivity Correction Factor 8 3 ak 5 R 3 z 0 0001 0 0002 0 0003 0 0004 0 0005 0 0006 0 0007 0 0008 0 0009 Reading Conductivity mmpy Slem Figure 2 Conductivity Correction Factor mmpy uS cm 24 9000 Plus Reference Manual Conductivity Correction Factor Corrosion Rate Multiplication Factor E pH amm A D HT 0 0 3 04 0 5 0 6 Reading Conductivity umpy pS cm CET TTL 1 2 0 9 Figure B 3 Conductivity Correction Factor uS cm 25 Appendix Manufacturer s Declaration of Conformity We the manufacturer hereby declare that this product PRODUCT NAME 9000 Plus Hand Held Portable CORRATER MODEL 9000 Plus is in full compliance with all applicable EU Product Directives and required standards as noted below DIRECTIVE 89 336 EEC PRODUCT STANDARDS Radiated Emissions EN 55011 1991 Group 1 Class A Immunity Heavy Industrial EN 50082 2 1995 Electrostatic Discharge EN 61000 4 2 1995 Radiated EM Field ENV 50140 1994 PLACE AND DATE OF ISSUE April 14 1997 Rohrback Cosasco Systems Santa Fe Springs California USA AUTHORIZED SIGNATURE J QA Ronald J Martinez Direc
12. an the corrosion rate or very erratic this is indicative of a significant pitting which should be verified by visual inspection of the probe electrodes Imbalance can be caused by several factors 1 Severe pitting Pitting is generally irregular and non uniform consequently the greater this irregularity or non uniformity the greater is the probability of imbalance between the two electrodes Pitting is generally accompanied by an increase in imbalance and also greater irregularity and fluctuation of the reading 2 Improper or inadequate inhibitor film formation Where filming inhibitors are used and are not established due to inadequate flow or quantity of inhibitor imbalance is greater and shows greater fluctuation This will often anticipate an increasing corrosion rate with reducing inhibitor film 3 Differential scaling or fouling of the electrode 4 Damage an electrode or a loosened electrode NOTE Imbalance readings will typically increase when corrosion rate values increase There should be concern for pitting when the imbalance increases significantly without a similar increase in corrosion rate 11 5 Maintenance Introduction Routine maintenance of 9000 Plus is not required except for battery replacement Probes however should be inspected at intervals and electrodes replaced when required If a problem is suspected with the 9000 Plus instrument the following tests can be performed to verify proper
13. anodic reaction Fe 2e this in an oxygen rich environment can be driven by the following cathodic reaction 2H20 4e 4 OH When large amounts of oxygen are available at a portion of a metal surface oxygen not only maintains this cathodic reaction but it promotes the reaction At other locations on the metal surface where oxygen 1 less available the anodic reaction proceeds to balance the cathodic reaction small intergranular cavity would represent an excellent site for the anodic reaction to take place because there is less available oxygen In the case of an iron alloy the reaction causes the rapid localized conversion of iron atoms to ferrous ions since a small anodic area can be supported by the larger cathodic area As this iron oxidation proceeds the small cavity grows which in turn exposes a larger iron surface that is essentially void of oxygen causing it to be a very active anode This process which has the natural tendency to accelerate describes the growth of a corrosion pit Since susceptible pitting sites tend to be randomly distributed and generally are not too numerous on a metal surface there is a high probability that on two seemingly identical metal electrodes one of the electrodes will have a greater number of susceptible pitting sites than the other electrode If these two electrodes are the electrodes of a two electrode CORRATER probe and they are submersed in a conductive solution which tends
14. current setting for engineering units Use the arrow keys to scroll through the three options When the desired option is displayed press the Set Mult key to save your selection and initiate normal operation 10 9000 Plus Reference Manual Interpretation of Operating Parameters and Reading Imbalance Readings Imbalance is often referred to as pitting tendency It is actually a sample of Electrochemical Current Noise ECN between the two electrodes when the electrodes are connected to a zero impedance ammeter effectively measuring the short circuit current The 9000 Plus measures this current and displays results in units of 0 5 LA per square centimeter of surface area of each electrode with mpy units and at a multiplier of 1 00 Regular electrodes are 5 0 square centimeters and therefore one imbalance or pitting unit is 2 5 uA of current with mpy units and at a multiplier of 1 00 Scaling of this reading is modified by the probe multiplier and metric unit conversion The purpose for this scaling is to make the imbalance reading meaningful when compared to the corrosion rate reading It has been found empirically that when the imbalance reading 15 less than the corrosion rate reading or close to zero corrosion is general corrosion with insignificant pitting If the imbalance becomes more erratic and similar to or greater than the corrosion rate value this is indicative of increased pitting If the imbalance is up to ten times greater th
15. epresent the most aggressive system corrosion rates Preferably they should be located where the liquid flow velocity past the electrode exceeds 1 foot per second 0 3 m sec if the requirement is to measure corrosion rates representative of a flowing environment Alignment of the electrodes relative to the direction of process flow is important to obtain reliable corrosion rate measurements Proper alignment is with the imaginary line connecting the centerlines of the two electrodes perpendicular to the direction of the process flow Refer to Figure 3 1 With this orientation one electrode does not shade the other electrode and both are subject to nearly the same corrosive environment probe 15 installed in an elbow fitting where flow changes direction position the probe so that the electrodes face the oncoming flow Refer to Figure 3 2 Flow Flow _ _ Recommended Not Recommended Figure3 1 Probe Orientation Relative to Flow 6 9000 Plus Reference Manual Flow Figure 3 2 Probe Orientation at a Tee Fitting Probe Connection The 9000 Plus is supplied with one coiled probe cable terminated in a 6 pin connector The connector is suitable for direct connection to all CORRATER probes The only exception is interconnection to a Model 6080 High Pressure CORRATER probe where a portable probe connecting adapter is also required Chapter 4 Operation Genera
16. er is reduced 1 32 inch 0 794 mm or more CORRATER electrodes are nominally 3 16 inch 4 76 mm diameter and 1 1 4 inch 31 75 mm in length when new As corrosion occurs on the electrodes their diameter decreases and begins to significantly affect the accuracy of the corrosion readings Do not use pliers when installing new or cleaned electrodes on a standard probe body They should be screwed onto each mounting stud only finger tight slightly compressing the rubber O rings at the base of the stud Handle the electrodes with a clean cloth or paper towel to avoid depositing any contaminating oily film In the event of contamination a suitable degreaser can be used to clean the electrodes Electrode Pretreatment Pretreatment of the electrodes may be done is some instances but is only recommended if the same type of treatment is used on the plant system whenever new material is installed Generally a full strength sample of the treatment chemical is used The new electrodes are carefully placed into the solution for a 6 12 hour period and then threaded onto the probe and placed into service Some systems employ an initial high level treatment procedure before the inhibitor rate 15 reduced to a maintenance level The treatment should be selected relative to the probe electrodes being used If the electrodes are installed without pretreatment the corrosion rate indicated will be that of which would occur on new material put in the system Thi
17. he test and auxiliary electrode do not correct for effects of solution resistance without special electronic solution resistance compensation With high to moderate conductivity environments this effect of solution resistance is not normally significant 3 2 9 Three electrode probes compensate for the solution resistance Rs by varying degrees depending on the position and proximity of the reference electrode to the test electrode With a close spaced reference electrode the effects of Rs can be reduced up to approximately ten fold This extends the operating range over which adequate determination of the polarization resistance can be made 20 9000 Plus Reference Manual 3 2 10 two electrode probe with electrochemical impedance measurement technique at high frequency short circuits the double layer capacitance so that a measurement of solution resistance Rs can be made for application as a correction This also extends the operating range over which adequate determination of polarization resistance can be made Imbalance or Pitting Index Metal surfaces no matter how uniform they may appear have numerous microscopic imperfections Metals such as iron alloys are crystalline in structure but surface imperfections such as small intergranular cavities tend to grow especially in liquids that have large concentrations of dissolved oxygen The corrosion processes iron oxidation for iron alloys can be described by the following
18. l When the 9000 Plus CORRATER instrument is turned on the software revision level is indicated followed by the battery voltage Once the initial setup of the instrument is performed the selections remain in effect until individually changed by the operator The 9000 Plus will retain the configured values when the unit is switched off and on and when batteries are replaced Figure 4 1 Front Panel of 9000 Plus 8 9000 Plus Reference Manual PUSH UP RELEASE BATTERY COVER Figure 4 2 Battery Compartment Configuration Operation of the instrument is accomplished via the front panel keys A description of each key and the function it performs follows Read Probe This key activates the measurement cycle The display will show the most recent corrosion rate and imbalance measurement Set Mult This key displays the beginning of a menu list of user definable multipliers Repeatedly pressing the arrow keys allows you to scroll through the list Pressing the SET MULT key a second time stores the menu selection and returns the unit to operation Up Down Arrow Keys These keys are used to scroll through the list of multipliers Initial setup requires the operator to choose the engineering units mpy mmpy umpy that will be used to display the corrosion rate on the screen see below Multip
19. lier List PROBE MULTIPLIER The alloy correction and geometry multipliers are selectable from the Set Mult menu Use the arrow keys to scroll through the following options and press the Set Mult key when the correct choice is displayed Mild Steel Admiralty Brass Copper 304 Stainless Steel 316 Stainless Steel 90 10 Copper Nickel 70 30 Copper Nickel Zinc Lead 1100 Aluminum 2024 Aluminum Flush Mild Steel 9 cm Area Mild Steel If it 15 necessary to check the current setting of the multiplier press the Set Mult key and the current setting is displayed If it is the desired selection press Set Mult again to return to normal operation If a measurement is taken with an incorrect multiplier simply change the multiplier to the desired option and the measurement on the display will be changed to the correct value Conversely when you change the multiplier for a new probe the displayed measurement will be inaccurate until a new measurement cycle is completed The factory default setting is at Mild Steel Initial Start Up Parameter List ENGINEERING UNITS The selectable units are mils per year mpy millimeters per year mmpy or micrometers per year The factory default is set at SETTING ENGINEERING UNITS The engineering unit menu is accessed by holding down both arrow keys simultaneously when the instrument is off and then applying power to the unit by pressing the on key The 9000 Plus will display the
20. mportant factor is that the electrodes should be REPRESENTATIVE of the conditions to be monitored New electrodes may be more responsive to changes in the corrosivity of the fluid Electrodes which have been in use for sometime will be more representative of corrosion rates of the more aged plant system material which will have some film build up 12 9000 Plus Reference Manual UNS Code Material Multiplier K03005 Pipe Grade Carbon Steel 1 00 A91100 Aluminum 1100 0 0 94 92024 Aluminum 2024 C11000 Copper 110 ETP Comm Pure 2 00 C44300 CDA 443 Arsenical Admiralty C44500 CDA 445 Phosphorized Adm C64200 CDA 642 A1 Silicon Bronze 10276 Hastelloy C276 R50400 ASTM B 348 Grades 2 4 Titanium 530400 AISI 304 Stainless Steel S31600 AISI 316 Stainless Steel 531603 AISI 3161 Stainless Steel S31803 2205 Duplex Stainless Steel 532750 2507 Duplex Stainless Steel 217001 Grades 1 2 3 or 5 Zinc Table 5 1 Corrater Multiplier Factors 13 NOTE These factors are stored in the memory and are accessed when setting the MULTIPLIER value as described in Section 4 Metallurgy Values are based upon use of CORRATER electrodes which have surface areas of 5cm for standard probes and 0 5 cm for flush probes When metallurgy is used that is not preprogrammed in the 9000 Plus select mild steel and manually multiply the factor below Electrodes should be replaced when the diamet
21. ont panel keys while monitoring the liquid crystal display A description of user definable parameters is given in the operation section of this manual and on a flow chart located on the back of the instrument In some cases initial setup will not be required since factory defaults have been set Chapter 2 Specifications Operational Input Single Channel Probe Corrosion Rate Ranges Autoranging 0 01 to 200 mpy Or 0 to 5 08 mmpy 0 to 5080 umpy Imbalance Ranges Pitting Index 0 01 to 100 pitting units Or 0 025 to 250 uA Probe Compatibility Two Electrode CORRATER Probe Three Electrode CORRATER Probe Probe Connectors 6 ft Coiled Cable with Standard 6 Pin Probe Connector 200 ft measurement capability Calibrated Probes One point calibrated test probe P N 011000 5 Measurement Cycle Time Factory set at 3 minutes polarization time is 1 minute Multiplier Range Menu driven for most common alloys and geometries Instrument Operating Temperature 32 F to 122 F 0 C to 55 C Instrument Storage Temperature 4 F to 131 F 20 C to 55 C 4 9000 Plus Reference Manual Operating Range Conductivity umhos cm divided by corrosion rate gt 4 Operating Range for 9000 Plus 1000 100 Non Operating Region 10 Typical Corrosion Rate of Carbon Steel 1 Operating Region 0 1 0 1 1 10 100 1000 10k 100k Conductivity uS cm or
22. s may typically take a few hours to a few days to decrease to the normal on going value Pretreatment may artificially protect the material so that it is unrepresentative of any new material that may be put in the system Correlation with Electrodes as Coupons Weigh the electrodes in the same manner as a coupon would be weighed on a balance scale graduated to 0 0001 gram before placing them in service The coupon should be placed into service at the same time After a 30 60 or 90 day period remove clean and analyze them in the same manner The readings from the instrument integrated over a period of time and the data from the electrodes and coupons should correlate 14 9000 Plus Reference Manual 15 Theory of Operation of CORRATER Systems CORRATER systems measure the instantaneous corrosion rate of a metal in a conductive fluid using the linear polarization resistance LPR measurement technique Corrosion is an electrochemical process in which electrons are transferred between anodic and cathodic areas on the corroding metal resulting in oxidation corrosion of the metal at the anode and reduction of cations in the fluid at the cathode Sterns and Geary originally demonstrated that the application of a small polarizing potential difference AE from the corrosion potential of a corroding electrode resulted in a measured current density imeas which is related to the corrosion current density
23. tor of Quality Assurance
24. umhos cm Normal operating range with direct reading Operating range with conductivity correction applied For extended operating range when conductivity is known use Conductivity Correction Factor for corrosion rate See method of calculation in Appendix B Display Liquid Crystal Display Two lines 12 characters per line Power Requirements One 9V DC Alkaline Battery Battery Life 10 hours continuous operation Unit Weight 14 ounces Certifications Complies with all applicable EU Product Directions 89 336 EEC 3 CORRATER Probe Installation The 9000 Plus is intended to be used with any standard 2 electrode CORRATER probes Three electrode probes can also be used but for simplicity and economy it is recommended that 2 electrode probes be used Probes with replaceable cylindrical electrodes are generally referred to as standard probes and probes with disc electrodes are referred to as flush probes because the electrodes are flush with the end surface of the probe The probes are available in many designs including fixed adjustable retractable and retrievable mounting configurations Also probe electrodes are available in many element and alloy materials The material selected should closely match the material of construction of the pipe or vessel for which corrosion information is desired Probes should be installed where corrosion is most likely to be greatest so that readings will truly r
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