USFilter FlowMAX FM Series, FlowMAX FS Series Operation And Maintenance Manual

Page 1
Operation and
Maintenance
FlowMAX
FM Series
FS Series
USFilter
10 Technology Drive
Lowell, MA 01851 USA
Tech Support (800) 783-7873
Customer Service (800) 466-7873
Single Pass
Reverse Osmosis Unit
Model # FMX-XX
Colorado Springs
Job # XXXXX
Rev. B Issue Date: 05/1999
P/N 68/S8601
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TABLE OF CONTENTS MAX RO MANUAL REV: B 05/1999
TABLE OF CONTENTS
SECTION DESCRIPTION PAGE
1.0 INTRODUCTION
1.1 Manual User’s Guide 1-1
1.2 Disclaimer Statement 1-2
1.3 Proprietary Rights Statement 1-2
1.4 Equipment Support 1-2
1.5 General Safety Guidelines 1-3
2.0 EQUIPMENT DESCRIPTION
2.1 General System Description 2-1
2.2 Theory of Reverse Osmosis 2-3
2.3 Mechanical Component Description 2-7
2.4 Electrical Component Description 2-9
2.5 Functional Description 2-13
3.0 INSTALLATION
3.1 Required Tools and Parts 3-1
3.2 Equipment Installation Guidelines 3-2
3.3 Equipment Installation Procedures 3-2
4.0 OPERATION
4.1 Initial Startup 4-1
4.2 Normal Operation 4-3
4.3 Short Term Shutdown Procedure 4-4
4.4 Long Term Shutdown Procedure 4-5
5.0 MAINTENANCE
5.1 Maintenance Schedule 5-1
5.2 Filter Cartridge Replacement 5-1
5.3 Membrane Element Replacement 5-2
5.4 Troubleshooting 5-4
5.5 Recommended Spare Parts 5-6
5.6 RO Membrane Element Long Term Storage Procedure 5-7
5.7 RO Membrane Element Cleaning 5-10
6.0 APPENDIX
6.1 RO Data Collection Form 6-1
6.2 RO Operating Specification Sheet 6-4
6.3 QA Data Sheet 6-6
6.4 Drawings 6-7
6.5 Component Manufacturers Literature 6-9
6.6 M.S.D.S Sheets 6-9
USFilter United States Filter Corporation
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INTRODUCTION FLOWMAX RO MANUAL REV: B 05/1999
1.0 INTRODUCTION
1.1 MANUAL USER’S GUIDE
This manual describes the procedures necessary to install, operate, and maintain your USFilter Reverse Osmosis System. Please read this manual carefully before installing and operating your equipment. The equipment warranty may be voided if installation or operation instructions are not followed correctly.
This manual has been formatted for ease of use, combining the instruction for the entire RO unit into one manual. Literature supplied with some major components being used on this equipment is provided in the back of this manual.
This manual is divided into six sections. The table of contents for these sections is located at the front of the manual. The pages within each section are numbered [section #]-[page #] with the page numbers starting at 1 and incrementing sequentially.
NOTE: Page numbering will skip over any special documents and continue on the page
following the document. Special documents will be noted with an introduction statement that is listed in the table of contents.
Warnings, Cautions, and Notes are used to attract attention to essential or critical information in a manual. Warnings and Cautions will appear before the text associated with them, and notes can appear either before or after associated text.
NOTE: Notes are used to add information, state exceptions, and point out areas that may
be of greater interest or importance.
Warnings indicate condition, practices, or procedures which must be observed to avoid personal injury or fatalities.
WARNING
Cautions indicate a situation that may cause damage or destruction of equipment or may pose a long term health hazard.
CAUTION
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1.2 DISCLAIMER STATEMENT
The operation and maintenance manual is intended to be used with the information provided in the component manufacturers literature, which is in the Appendix. These manuals should provide complete and accurate information to meet your operating and/or service requirements based on the information available at the time of publication. However, USFilter assumes no responsibility for the technical content of the component manufacturers literature.
The information in these manuals may not cover all operating details or variations or provide for all conditions in connection with installation, operation and maintenance. Should questions arise which are not answered specifically in this manual, contact the USFilter Service Department.
USFilter reserves the right to make engineering refinements that may not be reflected in these manuals. The material in these manuals is for informational purposes and is subject to change without notice.
1.3 PROPRIETARY RIGHTS STATEMENT
This manual discloses information in which USFilter has proprietary rights. Neither receipt nor possession of this manual confers or transfers any right to the client, and by its retention hereof, the client acknowledges that it will not reproduce or cause to be reproduced, in whole or in part, any such information except by written permission from USFilter. The client shall have the right to use and disclose to its employees the information contained herein for the purpose of operating and maintaining the USFilter equipment, and for no other purpose.
In the event the content of this manual is altered or section/items are omitted during a reproduction, in whole or in part, and instructions or definitions within the reproduction result in personal injury to those who follow the altered instructions, the burden of responsibility for personal injury falls solely on the party who affects the reproduction.
1.4 EQUIPMENT SUPPORT
USFilter continually strives to provide safe, efficient, trouble-free equipment using the optimum technology for your application. If problems should develop, USFilter ‘s worldwide network of technical support will be available to provide assistance. For service, sales, parts, or additional manual copies call your area representative or the number provided on the cover of this manual.
USFilter United States Filter Corporation
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1.5 GENERAL SAFETY GUIDELINES
This equipment operates at high voltage and high pressure, has moving parts
WARNING
and hazardous chemicals that may cause serious injury or fatality if not operated and maintained according to the procedures outlined in this manual.
1. No one should use or service this equipment without proper training and supervision. It is the responsibility of the owner to ensure that this equipment is used properly and safely, strictly following the instructions contained herein.
2. Remain alert at all times during the operation of this equipment. Do not get near this equipment if you are drowsy or impaired in any other way.
3. Always wear safety equipment (safety glasses, gloves) for protection while working on the equipment.
4. Refer to Material Safety Data Sheets prior to handling hazardous chemicals.
5. Always operate the equipment at the parameters specified.
6. Never connect the system to piping that has not been approved by USFilter. If there are any doubts, please call your USFilter local branch.
7. Never remove any components from the unit while under pressure.
8. No one under the age of 18 years of age should operate or be allowed near this equipment.
9. Warning labels have been placed on the equipment to remind the operator of certain hazards. Never remove these labels. If any warning label is illegible or missing, please contact U.S. Filter for a free replacement.
10. Proper maintenance assures the equipment will run properly and can lower the risk of injury. Be sure to follow the instructions on maintenance carefully.
11. Be sure to maintain all equipment, tools and sub-systems used with the equipment.
12. Continuously inspect the system for leaks and damage. Correcting problems as they occur will help prolong the life of the system.
13. Use Lock-Out and Tag-Out devices when servicing the unit.
14. This manual should be used as a guidance tool and should not replace common sense. If you are unsure about a procedure, ask your supervisor. USFilter welcomes any questions you may have. USFilter can arrange to provide on-site training if necessary.
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SAFETY PRECAUTIONS
The purpose of this manual is to provide the user with the necessary information to operate this equipment without undue risk. Failure to follow the instructions laid forth in this manual may put the operators at risk of injury and possible fatality. Please read this entire manual before beginning any procedure. This Operations and Maintenance Manual should remain with the equipment at all times, to act as a ready reference guide for anyone who operates this equipment.
SAFETY EQUIPMENT
Below is a list of equipment and materials that should be kept nearby the equipment. The equipment is the bare minimum required to maintain a safe working environment.
1. Lock-out and Tag-out devices for servicing and shutdowns.
2. Eyewash/safety shower for any chemical accidents.
3. Safety glasses are to be worn at all times.
4. Earplugs should be worn when encountering high levels of noise.
5. Gloves that offer protection from the chemicals used herein.
6. Steel toe work boots for protection against heavy equipment and components.
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2.0 EQUIPMENT DESCRIPTION
2.1 GENERAL SYSTEM DESCRIPTION
The purpose of this section is to introduce the user to the equipment. A thorough understanding of the equipment will help when installing, testing, and operating the system. Refer to the drawings supplied in the Appendix for further clarification.
MAX Membrane Systems are the standard 8” RO product line for USFilter . There are four different sub groups of MAX RO units, tailored to the specific needs of the pharmaceutical and beverage industry as well as general industrial and commercial applications. These are described below.
PharmMAX™
The PharmMAX™ RO system is packaged for the pharmaceutical and biotech industries. These units feature Filmtec RO-390-FF full fit membrane elements, Codeline FRP, 80A side port direct connect, pressure vessels, Grundfos CRN SST pumps and Allen Bradley PLC based control systems. We have three standard sizes available, with your choice of either PP or SST sanitary product piping. The feed piping is PVC, but SST piping is also available. These systems feature Thornton 200 series conductivity and flow monitors, and the new Fluidyne vortex shedding flow sensors. Another new feature is virtual product flow display, with flow sensors in the feed and reject lines, and no dirty intrusions into the product line. The Thornton 200F flow monitor allows you to display the product flow as the difference of the two measured flows. (For lower flow rates, please see the new Pharm40 Series of pharmaceutical RO units.) .
FlowMAX™
The FlowMAX™ RO system is packaged for general industrial applications. There are 10 different sizes that come standard with Filmtec BW30-365 membrane elements, Codeline FRP, 80A side port direct connect, pressure vessels. There are two standard pump choices, the T&T horizontal booster pump or the Grundfos BM series submersible pump. The standard control package is a Allen Bradley MicroLogix PLC control system. (There are standard SCL 5/04 and Remote I/O panels that can be used if required.) The feed piping and product piping are PVC. Like the PharmMAX™ , the FlowMAX™ systems feature Thornton 200 series conductivity and flow monitors, and the new Fluidyne vortex shedding flow sensors. The two piece frame design allow you flexibility in layout configurations, for jobs with limited floor space. Important to note that due to the different feed flow requirements, and depending on which membrane you select, the cartridge filter housing is not standard and mounted on the RO frame, so must be sized and ordered separately.
BevMAX™
The BevMAX™ RO system is packaged for the beverage industry or any application that requires all piping to be SST. They are similar to the FlowMAX, except all piping is mill finish 316L SST. These units are available with either Filmtec BW30-365 or BW30-440LE membrane elements, and Codeline FRP, side port, direct connect, pressure vessels. The feed pumps are all SST, T&T horizontal booster pumps. The standard control package is a AB MicroLogix PLC based control system. Like the other MAX RO systems, they feature Thornton 200 series conductivity and flow monitors, and the new Fluidyne vortex shedding flow sensors. Like the FlowMAX™, the cartridge filter housing is not mounted on the RO frame, and must be ordered separately.
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ValueMAX™
The ValueMAX™ RO system is packaged for commercial and general industrial applications. These are the most cost efficient standard 8” RO units available, for application where a sophisticated control system is not required. These units are available with either Filmtec BW30-365 or BW30-440LE membrane elements, and Codeline FRP, side port, direct connect, pressure vessels. The standard control package is a C2000 control system. The feed piping and product piping is PVC. The flow is measured with rotameters.
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2.2 THEORY OF REVERSE OSMOSIS
Water
Water exists in nature as a pure substance, but typically not in pure form. Many substances will readily combine with water. When water comes into contact with these substances they either become dissolved solids, such as minerals, gases and organic compounds or they become suspended solids such as clay, silt and micro-organisms.
Dissolved Solids
Mixtures containing dissolved solids are commonly called solutions. Solutions form when a solute material, such as salt (sodium chloride), becomes dissolved in a solvent, such as water. When a particle of salt contacts water, the salt disintegrates and spreads evenly throughout the water until the salt as a solid no longer exists. The salt molecules are still present, but they now exist in a liquid phase as part of the solution and are now referred to as dissolved ions. These ions carry either a positive or negative electrical charge, and will hereby be referred to as cations, if they carry a positive charge, and anions if they carry a negative charge.
Suspended Solids
Suspended solids, materials that do not dissolve in a solvent, exist as unevenly distributed particles in a mixture. Suspended solids larger than 5 microns are filtered out by the cartridge filters prior to the reverse osmosis membrane elements.
Ionic Content and Water Quality
The presence of ionic material (dissolved solids) in a solution, increases the solution's conductivity, or the ability to conduct electricity. Consequently, the use of a conductivity measurement device may be used as a means to approximate the amount of dissolved solids in a solution. The higher the conductivity potential of the solution, the higher the dissolved solids content. Unfortunately, the presence of dissolved and suspended solids may be detrimental to many water based operations, such as the production of steam for power generation, the rinsing of electronics components after manufacturing, and the preparation of food and pharmaceutical materials, just to mention a few. Consequently, these dissolved and suspended solids must be removed from the water prior to use in these and many other applications. One effective method of removing the majority of these contaminants is referred to as Reverse Osmosis.
Osmosis
Osmosis is a natural phenomenon that occurs when two solutions with different concentrations of dissolved solutions are separated by a SEMI-PERMEABLE MEMBRANE. In natural osmosis, the solvent or water in this application travels through the membrane from the solution with the lower concentration of ionic materials to the solution with the higher ionic concentration. This process continues until the ionic concentration of both solutions is equal or until the resultant passage of the water through the membrane reaches the osmotic pressure of the solution if the solutions are trapped in a container.
Reverse Osmosis
Reverse Osmosis is the reversal of this natural phenomenon, by the application of external pressure on the solution that contains the higher concentration of dissolved ions, thus forcing
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water through the semi-permeable membrane in the opposite direction, leaving behind the dissolved ions and the suspended solids. In the Reverse Osmosis process, the water that passes through the membrane is commonly referred to as permeate, or product, water. The water that remains behind the membrane along with the dissolved and suspended solids is referred to as the reject, brine, or reject water.
The table below gives some approximate osmotic pressure values as an example of how much pressure must be applied to the solution with a greater ionic concentration before any water will pass through a membrane into a solution containing a lesser ionic concentration.
SODIUM CHLORIDE CONC. APPROX. OSMOTIC PRESSURE
100 PPM 1 PSIG
1,000 PPM 11 PSIG
10,000 PPM (brackish water) 110 PSIG
35,000 PPM (sea water) 350 PSIG
It is impractical to convert all of the water processed to product water for several reasons including the osmotic pressure which develops as a result of the concentration of the dissolved ions which accumulate on the one side of the membrane, and the inability to keep the membrane free from suspended solids that would foul the surface of the membrane if not removed.
The rate of product water passage (or productivity) through the membrane is referred to as the flux rate and is generally expressed in "gallons per square foot of membrane surface per day" or in "gallons per day per reverse osmosis cartridge". The flux rate of a particular membrane is generally limited by several factors including: temperature, operating pressure, and the surface flushing action to keep the membrane surface free of suspended solids.
The rate of recovery of feed water converted into product water is generally expressed in the form of a percentage, with the ratio of product water being expressed as the recovery rate. For example if the feed flow rate to the RO unit is 200 GPM and the product rate from the RO unit is 150 GPM the rate of recovery would be expressed as 75%. The remaining 50 GPM did not pass through the membrane. It is referred to as the reject water and would be discarded (i.e., not recovered).
Membrane rejection is an expression of the ability to restrict the passage of dissolved ions through the membrane, and is generally expressed as a percentage. That is, if the feed water to the membrane contains 100 PPM of dissolved solids, and the resulting product water contains only 2 PPM of dissolved solids after processing, the resultant dissolved ions rejection rate is 98%. The opposite of this expression is also sometimes used and is known as the salt passage rate, which, for our example, would equal a rate of 2%. A membrane rejection rate of 100% is not practical due to imperfections in the membrane and the construction of the membrane element.
Practical Applications
Reverse osmosis becomes practical for water treatment when synthetic, semi-permeable membrane material is packaged in a suitable membrane element. Typically the elements are
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constructed of one of two classifications of membrane material, including cellulose acetate or triacetate, or some type of plastic based material such as a polyamide or polysulfone based material. These materials are then arranged into one of four element configurations including flat plate, tubular, hollow fiber or spiral wound, with the latter two configurations being most common in today's technology. Selection of the membrane material and element configuration are based on numerous factors including water chemistry, space limitations, product water quality requirements and system pre-treatment design. For this discussion, only the spiral wound element configuration will be described, based on the design of the RO unit covered by this Manual.
The spiral wound membrane configuration is constructed from a flat sheet membrane that is first folded and sealed to form an envelop, with one opened end. Porous backing material, placed inside the envelope separates the membrane sheets and forms a flow channel between them. The opened end of the envelope is then attached and sealed around a plastic product tube that is perforated, which allows the product water, or permeate, to pass into the product tube.
For compactness, the envelope of membrane material is then wrapped around the product tube in a spiral wound fashion with a coarse plastic screen, referred to as a brine channel screen, being included in the wrap, which creates a flow channel between the surfaces of the membrane where the feed water enters the element and the reject, or brine flow, passes out of the element. The element is then covered with an outer wrap of semi-rigid fiberglass for protection and to assist in maintaining a uniform round shape. The final dimensions of the element are usually approximately 40" long by either 4" or 8" in diameter.
The elements are then put into one or more cylindrical pressure vessels, which can contain one to six membrane elements depending on the unit design.
Pressurized feed water is introduced into one end of the vessel. Some of the water, driven by the feed pressure through the RO pressure vessel feed port, permeates through the membrane and passes into the product tube and exits the pressure vessel from the pressure vessel product port as product water, less most of the dissolved solids and all of the suspended solids. The remainder of the water passes along the surface of the membrane with the rejected dissolved and suspended solids and passes out of the pressure vessel as reject, or reject flow, from the pressure vessel reject port.
The pressure vessels are generally arranged in stages when more product water is desired than one vessel can produce. The staging of the vessels is designed to optimize the water flow patterns across the surface of the membranes. This uniform water flow promotes good flushing velocity across the membrane surface to prevent the accumulation of suspended solids on the surface which would then foul the membrane and reduce the productivity. Multiple stages are referred to as arrays.
A simple example of an array would be a unit containing three vessels, with two vessels plumbed in parallel in the first stage and the third vessel plumbed in series after the first two vessels in the second stage. In this case, the feed water to the unit is first split into two streams with each half being directed into one of the first stage vessels. On entering these two vessels, some product
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water is produced from each and collected from the two pressure vessel product ports, which are connected together outside of the pressure vessel in a common product water header. The water that is not recovered is passed out of the vessels as reject, along with the dissolved and suspended solids. This water is then collected into a common first stage reject header ( or reject header) and directed to the feed of the third vessel which is plumbed in series behind the first two vessels, where the process is again repeated. The second stage product is added to the first stage product. The second stage reject is directed through a control valve and disposed of along with most of the dissolved and suspended solids.
Recovery Limitations
As previously described, product recovery is the ratio of water volume recovered as product water compared to the volume of water supplied to the RO unit as feed water. Naturally, in an ideal situation you would like to recover all of the water, but this is not practical for several reasons as described below.
If all of the water that was processed were converted to product water, there would be no water available to flush the membrane surface area free of remaining suspended solids. Consequently, the suspended solids would build up on the surface of the membrane and gradually restrict the flow of product water until no permeate or product water could be produced.
The presence of some dissolved solids such as silica, barium, strontium or calcium and magnesium when present with carbonate or sulfate ions restricts the recovery of an RO unit more than other dissolved solids, due to their limited solubility in water. For example, the presence of silica (SiO2) in the feed water is often times the limiting factor in RO recovery, because it starts
to precipitate out of solution when it reaches a concentration of 100-120 PPM. That means that if the feed water contains 30 PPM of SiO2 then the recovery of product water is limited to about
75%, because the SiO2 concentration will be increased by 4 times which will result in a silica
concentration in the RO reject of approximately 120 PPM which is the limit of it's solubility. If you tried to recover 80% of the water, the concentration of SiO2 would reach 5 times the feed
water concentration or approximately 150 PPM and start to precipitate, fouling the membrane surface.
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2.3 MECHANICAL COMPONENT DESCRIPTION
The major mechanical components that make up the RO unit are described below.
Automatic Feed Water Control Valve
An automatic valve is mounted in the RO unit feed piping. This valve will shut off flow to the unit when it shuts down. A solenoid valve mounted in the Control Panel controls the operation of this valve. The solenoid requires 80 PSIG instrument air from an external source.
Feed Pressure Gauge
The line pressure from the filter inlet is displayed on a 0-100 PSI pressure gauge. The gauge has a 100mm stainless steel case, and is constructed of all stainless steel wetted parts and is glycerin filled.
High Pressure Pump
The RO unit has a high pressure booster pump mounted to the frame to boost the feed water to the required operating pressure for the reverse osmosis membranes. The pump is a vertical or horizontal, multi-stage type with stainless steel construction of all wetted parts. The pump is designed to provide the pressure and flow necessary to operate the system, with additional pressure available to allow for fouling or a minor decrease in feed water temperature. The FlowMax Series RO units are also available with a submersible multi stage pump with stainless steel impellers.
Low Feed Pressure Switch
A low feed water pressure switch is provided to protect the pump. It is adjusted to shutdown the RO unit if the inlet feed water pressure drops below the setpoint. The switch is wired through a delay timer to allow short pressure drops such as those that occur when the pump starts up.
Pump Discharge Throttling Valve
The water discharged from the high pressure pump is regulated by a stainless steel ball valve. By adjusting the position of the valve, you can regulate the flow and pressure feeding the first stage pressure vessels of the RO unit. The valve is also equiped with a locking device, which must be used to maintian correct valve position.
Pump Discharge Pressure Gauge
The outlet pressure from the high pressure pump is displayed on a 0-600 PSI pressure indicator. This gauge has a 63mm stainless steel case, and is constructed of all stainless steel wetted parts, and is glycerin filled. An isolation valve between the manifold and gauge allows you to operate the RO unit while isolating the gauge from the high pressure.
Pump Discharge Pressure Switch
A high discharge pressure switch is provided to protect the downstream components of the system from excess pressure. It is adjusted to shutdown the RO unit immediately if the pump discharge pressure exceeds the setpoint.
High Pressure Manifold
The pressurized feed water is piped through 316L stainless steel high pressure manifolding. The
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manifold is constructed of butt welded Schedule 10 fittings and pipe. The manifold sections are joined by flexible couplings, that are painted with polyurethane paint to match the frame. A cleaning connection is supplied on each interstage header and capped over with a stainless steel blind plug and flexible coupling. A half coupling on each interstage header is provided to connect to the interstage pressure gauge. The manifold sections are designed to accommodate future expansion of the system with minimum rework.
Reverse Osmosis Pressure Vessels
The RO unit has 8" round pressure vessels mounted to the frame. The vessels are constructed of fiberglass. The side ported vessels are close coupled to reduce manifolding. The inlet and outlet connections are 316L stainless steel with groove type connections. The vessels are built to ASME specifications, but are not code stamped.
Reverse Osmosis Membrane Elements
The RO unit is designed for 8" x 40" reverse osmosis membrane elements housed in pressure vessels on the frame. The standard elements are constructed of Thin Film Composite (TFC) membrane material. The membranes are designed to reject over 98% of the dissolved solids and over 99% of the suspended solids and organic material.
Reject Throttling Valves
The reject flow back pressure is regulated by two valves. One is a stainless steel ball valve and the other is a stainless steel globe valve. These valves are used to control the differential pressure across the membrane surface which in turn regulates the recovery rate of the system.
Interstage Pressure Gauge
The feed pressure from each high pressure feed manifold and the final reject line are displayed on a 0-400 PSI pressure gauge, located on the interstage SST header. The gauge has a 63mm stainless steel case, and is constructed of all SST wetted parts and is glycerin filled.
Feed & Product Piping
The feed and product piping for the FlowMax unit is PVC Schedule 80. The feed piping for the PharmMax unit is PVC Schedule 80, the product piping is sanitary PP or SST. The feed and product piping for the FlowMax unit is 316L SST.
Sample Valves
There is a sample valve on the product line of each pressure vessel. These valves provide an opportunity to analyze the product water flowing from each pressure vessel. The location of these valves permit the operator to isolate the product water of a vessel from that of all other vessels.
There is a sample valve on the common product line of the RO. This valve provides an opportunity to analyze the final combined product water flowing from the RO membranes.
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2.4 ELECTRICAL COMPONENT DESCRIPTION
Control Panel
The frame mounted Control Panel is U.L. listed. It houses the main disconnect switch, PLC, solenoid valves and alarm horn The door of the Control Panel contains the disconnect switch handle, system hour meter, % rejection monitor, flow monitors, and the switches and indicator lights.
Starter Panel
The frame mounted Starter Panel is U.L. listed. It houses the motor circuit protector, motor starter and overload. The door of the Starter Panel contains the disconnect switch handle. If the submersible pump is selected, there may be a motor protection device designated CU-3. This device is not U.L. Listed.
COMPONENT DESCRIPTION
Motor Circuit Protector
The main disconnect switch for the Control Panel is a motor circuit protector. This replaces the standard disconnect and motor fuses. It will trip when the Maximum amperage rating is exceeded and can be manually reset. This switch serves as the main power disconnect to the Control Panel.
Circuit Breaker
The low voltage components inside the Control Panel are protected with a 5 Amp circuit breaker.
Ground Fault Circuit Interrupter
A Ground Fault Circuit Interrupter (GFCI) is installed in the Control Panel to protect the instrumentation. This is required for non U.L. devices mounted in a U.L. Listed Control Panel.
Flowmeters
There are two flow sensors and one flow monitor on the RO unit. They will display the flow rates for the product and reject flows. They consist of an in-line vortex shedding flow sensor in the feed and reject line, and a digital monitor in the Control Panel. The monitors will display the flow in GPM, or other international units, and will also monitor and display the totalized flow. The 4-20mA outputs from the monitors are wired to terminals for data acquisition if required.
% Rejection Monitor
A percent rejection monitor is provided to indicate the overall system rejection of dissolved solids in the feedwater. The monitor will alarm if the product water quality is out of limits for more than 5 minutes, in which case the unit will shut down on low quality. The 4-20mA output from the monitor are wired to terminals for data acquisition if required.
Alarm Horn
An alarm horn is mounted to the bottom of the Control Panel to
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give an audible warning during an alarm status condition.
Elapsed Time Meter
An elapsed time meter is mounted in the door of the Control Panel and will record the total hours the unit has run. This is important for maintenance and service scheduling.
High Pump Discharge Pressure Switch
A High pump discharge pressure switch can be mounted on the Control Panel. It is adjusted to shutdown the RO unit if the pump discharge pressure rises above the setpoint. This will prevent the pressure vessels from the possibility of over pressurization.
2.5 FUNCTIONAL DESCRIPTION
Below is a description of the function of the major system components and the features of the MAX RO unit.
Feed Inlet Valve V-2
When the HOA switch is turned to AUTO or HAND, solenoid valve SV-1 will energize and the feed water inlet valve will open. It will remain open during operation and remain open for an additional 60 seconds after the RO pump stops. The valve will not open if the pre-treatment lockout signal is active, or if the call for water signal is inactive.
Feedwater Flow Sensor FE-1
The flow sensor in the feed line will send a pulse signal to the flow monitor. The feed flow will be displayed on the secondary display line, accessible by pressing the button on the monitor.
Feedwater Low Pressure Switch PSL-1
The pressure switch in the feed line will protect the RO unit high pressure pump from cavitation if the feed pressure drops and remains below 10 PSIG for more than 10 seconds. As soon as the alarm initiates, the LOW FEED PRESSURE light will start to flash. After the 10 second delay, the RO unit will stop and the alarm horn will sound. The 10 second delay is to accommodate a momentary pressure drop when the pump first starts up.
Feed Conductivity Sensor CE-1
A feed conductivity sensor will measure the conductance of the feed water and send a signal to the conductivity monitor in the Control Panel. The sensor has a 0.1/cm constant. The feed conductivity reading is used to calculate the system rejection.
Feedwater Temperature Shutdown
The RTD in the feed conductivity sensor is used to measure the feedwater temperature. This value is displayed on the conductivity monitor. If the operating feed temperature (user defined) is out of range, the alarm initiates, the HIGH FEED TEMPERATURE light will start to flash, and the unit will shut down. There is no time delay, this is an instantaneous shutdown. For standard TFC membranes, this switch will be set to 100 degrees F.
High Pressure Pump
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The pump will start 60 seconds after the HOA switch is turned to HAND or AUTO. If the feed pressure does not rise above the required 10 PSI, the pump will not start. The pump will not start if the pre­treatment lockout signal is active, or if the call for water signal is inactive.
Pump Discharge High Pressure Switch PSH-1
The pressure switch located on the pump discharge manifold will shutdown the RO unit if the pressure exceeds the safe operating limits of the system. As soon as the alarm initiates, the HIGH DISCHARGE PRESSURE light will start to flash and the RO unit will stop. There is no time delay, this is an instantaneous shutdown. On the standard systems it is set to 300 PSIG.
Product Conductivity Sensor CE-2
A product (permeate) conductivity sensor will measure the conductance of the product water and send a signal to the conductivity monitor in the Control Panel. The sensor has a 0.1/cm constant. The product conductivity reading is used to calculate the system rejection. The product and feed conductivity readings are used to calculate membrane rejection, which is displayed as percent rejection on the monitor. If the percent rejection value drops and stays below the setpoint (factory set at 96%), for five minutes, the unit will shut down. The time delay gives the unit time to rinse up to quality upon start up.
Low Quality Alarm CIT-1
Whenever the percent rejection value is below the setpoint, the LOW QUALITY light will flash and a five minute time delay begins. Whenever the LOW QUALITY light is flashing, the product divert to drain valve will be opened. (note the product divert to drain valve is not included on the RO unit, but must be installed in the field. If it is not installed, activation of SV-2 will have no effect on the system.) This will keep low quality permeate water out of the storage tank. When the quality rises above the setpoint, SV-3 will energize and open the product to storage tank valve, and after a 10 second time delay, SV-2 will de-energize and close the product divert valve. The 10 second time delay is incorporated to give the storage tank valve time to open before the divert valve closes.
Reject Flow Sensor FE-1
The flow sensor in the reject line will send a pulse signal to the flow monitor. The reject flow will be displayed on the primary display line of the quality monitor CIT-1.
Flow Monitor FIT-1
The flow monitor will take the two flow signals from the feed and reject lines, and calculate the product flow. (Feed flow minus reject flow equals product flow.) The monitor is completely programmable by the user to adjust alarm set points and display readings. The factory default display will show product flow and reject flow on the primary display, and feed flow on the secondary display. The 4-20-mA outputs from the monitor for product flow and reject flow will be wired to terminals in the panel in the event these signals are needed. The two relay alarm outputs will be used to shut down the RO if the product or reject flows are out of range.
Flow Alarm FIT-1
The flow monitor has two relay outputs that will go into the PLC to alarm on Low Reject Flow and on High Product Flow. If the flow is more than 5% above the recommended product flow or 5% below the recommended reject flow, the Flow Alarm light will flash and a two minute timer starts. If the flow stays out of range for more than two minutes, the RO unit will shut down. Incorrect flows will cause
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EQUIPMENT DESCRIPTION FLOWMAX RO MANUAL REV: B 05/1999
irreversible damage to the membranes, and void the warranty.
RO Product to Storage Tank Valve V-9
This valve is not include on the RO, but should be installed in the field as close to the storage tank as possible. This allows the product piping to be rinsed to drain upon start up. It should be an air actuated type, normally closed (fail closed) valve. The sequence of this valve is described above under Low Quality Alarm CIT-1.
RO Product to Drain Valve V-10
This valve is not included on the RO, but should be installed in the field as close to the storage tank valve V-9 as possible. There must not be any back-pressure on the drain piping after this valve. It should be an air actuated type, normally open (fail open) valve. The sequence of operation for this valve is described above under Low Quality Alarm CIT-1.
Note: If the product valves are not installed, the air outlets on the control panel
for SV-2 & 3 will need to plugged.
Auto Flush Mode
A “MANUAL-OFF-AUTO” selector switch allows you to select one of three modes:
1. MANUAL-manually hold open the product divert valve
2. OFF-de activate the 2 hour auto flush mode
3. AUTO-activate the 2 hour auto flush mode
When the selector switch is put in the MANUAL position, the product to drain valve (V-10) will open and stay open until taken out of the MANUAL position. When the switch is in the AUTO position, a two hour timer is initiated each time the RO shuts down. If the RO has not automatically restarted within the two hours, the RO will automatically start up and run product to drain for 5 minutes, then return to the standby mode, and the two hour timer is again initiated.
When the switch is in the OFF position, the autoflush will not be activated. If the product divert valves are not installed in the product line as noted above, this selector switch must be in the OFF or MANUAL position only, or the RO could start up for five minutes every two hours and overfill the storage tank.
Pretreatment Lock Out
There is a relay in the control panel that can be tied into the pretreatment system to shutdown the RO in the event of an interruption in the feedwater supply. (This is typically caused by softener going into regeneration or multi media filters going into backwash.) When a signal from the pretreatment occurs, the RO will shutdown and go into a standby mode. At this time the PRETREATMENT LOCKOUT light on the panel will be flashing. The RO will automatically re-start upon de-activation of the signal from the pretreatment equipment. If there is no pretreatment interlock required, the terminals in the control panel need to have a jumper wire connected across them. If the RO is run in the HAND mode, the pretreatment interlock will be ignored. A loss of feed water will cause the unit to shut down on low feed pressure.
Hand-Off-Auto Switch (HOA)
Hand
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EQUIPMENT DESCRIPTION FLOWMAX RO MANUAL REV: B 05/1999
When the HOA switch is turned to HAND position, the RO unit will run and remain running until the switch is turned back to the OFF or any of the following alarm conditions; low feed pressure, high feedwater temperature or high pump discharge pressure. This operating mode completely bypasses the shutdown signals from the pretreatment system, storage tank level sensing device or low product quality alarm.. This mode is typically used for initial start-up rinse or after a cleaning cycle to rinse up the membrane elements.
Off
Turning the HOA switch to the OFF position at any time will stop the RO pump and the unit will remain off until the switch is placed into the HAND or AUTO position.
Auto
When the HOA switch is turned to AUTO position, the RO unit will run and remain running until a shutdown signal is received for the pretreatment system or storage tank level sensing device. The unit will also shutdown based on any of the following alarm conditions; low feed pressure, high feedwater temperature, high pump discharge pressure, or low product quality. This is the position to be used for normal operation of the RO unit.
Storage Tank Full Light
There is a relay in the control panel that must be tied into storage tank level device. This is typically a pressure switch with a deadband or a set of level switches. The level sensing devices are used to start the RO when the tank level drops to half full, and stop the RO when the tank is full. It is important to maintain a deadband to prevent frequent cycling on and off of the RO unit. The level sensing device must have a set of normally closed dry contacts to connect to the RO control panel. The RO can not be run in the AUTO mode unless the level device is wired in. . If the RO is run in the HAND mode, the storage tank level device shutdown interlock will be ignored. This could cause the tank to overflow and possibly damage surrounding equipment.
Alarm Reset
After pressing the Alarm Silence pushbutton to silence the alarm, you must determine and correct the cause of the alarm. After this has been done, you must reset the panel prior to restarting the RO. To do this, turn the RO HOA switch to OFF, this will reset the panel and the alarm light will go off.. To restart the RO, turn the HOA switch to HAND or AUTO.
Alarm Lights
The alarm lights will flash off & on during an alarm condition, and they will continue to flash until the operator acknowledges the alarm. This is done by pushing the Alarm Reset pushbutton switch. After the alarm has been acknowledged, the light will remain on until the HOA switch is turned to the OFF position.
Alarm Horn
An alarm horn will sound whenever the unit shuts down based on the following conditions; ; low feed pressure, low reject flow, high product flow, high feedwater temperature or high pump discharge pressure. The alarm horn is silenced by pressing the Alarm Silence pushbutton switch. The alarm horn is controlled by a timer that will shut it off automatically after 5 minutes, in the event it has not been acknowledged. It will come back on after five minutes and sound for 30 seconds, then go off again. This cycle will continue until the Alarm Silence pushbutton switch has been pushed.
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EQUIPMENT DESCRIPTION FLOWMAX RO MANUAL REV: B 05/1999
Chemical Pump Receptacles
There are four 120 volt chemical receptacles mounted of the side of the RO Control Panel. They are used to power chemical injection pumps if these are used in the pretreatment system. The two receptacles labeled “Bisulfite” and “Acid/Caustic” will energize whenever the feedwater valve is on. The receptacle labeled “ antiscalant” will only be energized when the OR pump is running. The fourth receptacle is a convenience receptacle that can be used to power a PC or test instrument. This receptacle is always hot, as long as the circuit breaker inside the control panel is on. The service on the convenience receptacle is limited to 10 amps.
Auxiliary Contacts
There are two sets of auxiliary contacts in the panel that can be hooked up to remote devices. One is energized whenever the pump is running, the second is energized during alarm fault conditions.
Optional pH Monitor
An optional pH monitor can be supplied to monitor the feed water pH, and shut down the RO if the pH goes out of range. This alarm includes a 5 minute time delay, similar to the quality monitor. The pH monitor is located in a separate panel, and the alarm is wired back the Control Panel.
Electrical Controls Summary
Shutdown alarms Low quality product
Low feed pressure Flow Alarm High pump discharge pressure High feed water temperature
Status indicator lights Low feed pressure
Low quality Flow Alarm High pump discharge pressure High feed water temperature Product divert to drain valve open Pretreatment lockout Storage Tank Full
Switches RO Run Hand-Off-Auto (HOA)
Alarm Silence Auto Flush Selector Manual-Off-Auto (MOA)
Miscellaneous controls Elapsed run time indicator
Alarm horn Chemical pump receptacles
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EQUIPMENT DESCRIPTION FLOWMAX RO MANUAL REV: B 05/1999
Valve Sequence Chart
RUN MODE
RO Off Off RO start – quality below setpoint – start up rinse Off RO start – quality above setpoint – normal operation On Product water quality fault time delay On RO stop - 60 second time delay Off RO in standby mode – HOA in AUTO position Off RO in autoflush mode – HOA in AUTO position On RO out of Service Off
{-fully open }-partially open z-closed
PUMP V1 V2 V3 V4 V5 V6 V7 V8 V9 V10 V11
V1 optional main shutoff valve located off skid, supplied in field V2 automatic feed water shut off valve V3 feedwater sample valve V4 pump discharge throttling valve V5 interstage sample valves, one per stage V6 final product sample valve V7 reject throttling valve V8 manual reject throttling valve bypass valve V9 product to storage tank valve (located off skid) V10 product to drain valve (located off skid) V11 reject recycle throttling valve (3M systems only)
{zz}z z}}z{} {{z }z z}} z{} {{z}zz}}{z} {{z }z z}} z{} {{z }z z}} z{} {zz}z z}}z{} {zz}z z}}z{}
zzzzzzzzz{z
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EQUIPMENT DESCRIPTION FLOWMAX RO MANUAL REV: B 05/1999
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SECTION 3-1
INSTALLATION FLOWMAX RO MANUAL REV: B 05/1999
3.0 INSTALLATION
The purpose of this section is to provide general information on installation of new equipment. All equipment must be installed according to applicable codes. Refer to the Equipment Specification drawing supplied in the Appendix to ensure there is adequate support and clearance around the RO unit.
Installation of the U.S. Filter MAX RO unit consists of the following steps:
1. Uncrate and move the unit to the installation site.
2. Anchor the skid to the foundation.
3. Install the feed, product and reject plumbing lines.
4. Connect the electrical high voltage power wiring.
5. Connect control device wiring.
6. Connect air supply to solenoid valve.
7. Install any pre-treatment equipment and interlock to RO unit.
8. Install any post-treatment equipment and/or storage tank and interlock to RO unit.
3.1 REQUIRED TOOLS AND PARTS
The tools and parts specified in this section are the bare minimum required to install the RO unit at the site. The use of other tools and parts may be necessary, depending on the location chosen and other parameters.
Required Tools
Lock-Out/Tag-Out equipment safety glasses, gloves, earplugs moving equipment hammer drill with masonry bit pipe cutting, bending, gluing equipment electrical multi-meter
Required Parts
concrete anchor bolts (size determined by local seismic calculations). plumbing and electrical materials as required regulated air supply line automatic valves for auto flush feature product pressure relief valve
3.2 EQUIPMENT INSTALLATION GUIDELINES
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INSTALLATION FLOWMAX RO MANUAL REV: B 05/1999
1. All lifting and moving procedures must be performed by experienced construction workers using standard rigging methods.
2. Before beginning any equipment handling procedures, refer to the appropriate sections in the Occupational Health and Safety Administration (OSHA) manual #2206: “General Industry Standards.” Also, refer to any other applicable literature and information for cranes, lift trucks, and other equipment used for lifting and moving.
Damaged lifting devices can fail in service and cause severe personal injury
WARNING
and/or equipment damage. Never use slings or cables that are cut, frayed or kinked. Refer to OSHA manual #2206 for information on inspecting lifting devices for damage.
3. Make sure all equipment used for lifting and moving is properly maintained and is in good repair.
4. Be sure that components being lifted are balanced and will not tip or slip out of the lifting device.
5. When moving components with a forklift, be careful not to damage components.
6. Avoid “ramming” the lifting forks under pieces; use a crane or pry bar to lift the piece up enough to drive the forks under.
3.3 EQUIPMENT INSTALLATION PROCEDURES
1. Locate a level, flat, clean, hard surface, capable of supporting the weight of the RO unit. Refer to the Equipment Specification Drawing to determine the floor loading requirements and the service access space requirements for the unit.
NOTE: This area should have a local floor drain to carry away water which will fall to the floor
during operation, testing, and servicing this equipment.
2. Lay out the area that the RO System will occupy.
WARNING
Improper handling procedures can damage equipment and/or cause possible injury or fatality.
3. Move the RO unit to the location laid down in the previous step.
WARNING
Safety equipment should be worn at all times to avoid personal injury while securing equipment.
4. Drill holes in the pad through the frame tie down holes.
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5. Level the RO unit by installing shim stock under the frame near the frame tie down holes.
6. Install the anchor bolts and secure the frame to the anchor bolts using flat washers, lock washers, and nuts.
WARNING
Do not use the RO unit to support external piping. All plumbing runs should be supported per manufacturers’ recommendations and local codes.
7. Install the feed water plumbing line. The plumbing runs should never be smaller than the actual RO inlet pipe size, and may need to be larger for pipe runs over 50 feet.
NOTE: The plumbing materials should be of non-corroding materials (PVC, SST, etc.) Use of
this material will reduce the tendency to foul the membranes from metal precipitation.
8. Install the product water plumbing line. For the Auto Flush feature, two automatic valves should be installed in this line near the storage tank. (See P&ID) This will allow the RO unit to rinse the piping to drain during start-up.
NOTE: If this feature is used, install a pressure relief valve between the RO and the automatic
valves. Also it is recommended to install a manual divert to drain line for use during cleaning cycles.
9. Install the reject, or reject line directly to an open drain.
NOTE: As a general rule, no valves should be installed in this line. If necessary, install a relief
valve set at no greater than 5 PSIG. The valve should be directed to a visible drain so relief is obvious.
If the reject drain is below the level of the RO unit, install a vacuum breaker valve or open pipe leg on the reject line. This will prevent siphoning of all water out of the RO unit during shutdown.
10. Install a tank level sensing device with an adjustable deadband. We recommend a pressure switch with inches of water scale. The deadband will prevent frequent start/stop action of the system during run time.
11. Connect a regulated air supply to the inlet port of the solenoid on the bottom of the Control Panel. The air pressure needs to be 80 to 100 PSIG.
The plumbing installation should now be complete. Check the plumbing to ensure all joints are properly connected and supported.
Electrical Installation
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INSTALLATION FLOWMAX RO MANUAL REV: B 05/1999
WARNING
1. Employ a Lock Out Device and Lock Out Tag on the RO unit disconnect switch, located
CAUTION
2. Run electrical conduit for the high voltage power supply between the Control Panel and
3. Run electrical conduit between the Control Panel and any pre-treatment equipment lock-
4. Run electrical conduit between the Control Panel and the product water storage tank level
The following steps consist of electrical work to be performed by a qualified electrician only.
on the front of the Control Panel. Do not energize the main power at this time.
Support all conduit runs per local code requirements and to the conduit manufacturers recommendations. Improperly supported lines could cause equipment failure.
the main power supply.
out relays. If there is no pre-treatment equipment in the system, the terminals in the Control Panel need to be jumpered.. Refer to the electrical schematic drawing in the Appendix for terminal numbers. The unit will not run without this jumper.
sensing device.
5. Run electrical conduit between the Control Panel and the chemical injection pumps. If the chemical pumps have plugs, use the simplex receptacles mounted on the side of the Control Panel. The three different chemical pump receptacles energize at different times.
6. Verify that all electrical connections are secure and wired per the electrical schematic.
7. Remove the Lock-Out / Tag-Out equipment from the main power supply for the RO unit, and energize the circuit.
8. Verify that the voltage supplied is correct and matches the Voltage Identification Tag on the pump motor and inside the Control Panel.
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SECTION 4-1
OPERATION FLOWMAX RO MANUAL REV: B 05/1999
4.0 OPERATION
4.1 INITIAL STARTUP
The following procedure should be performed for the initial startup of the RO System or to restart the system if it has been idle and secured for a long term shutdown.
Required Equipment and Materials
Lock-Out and Tag-Out equipment Personal safety equipment, such as safety glasses and gloves Prefilter cartridge elements portable TDS monitor Chlorine test kit Portable pH meter
Pre-Startup Checklist:
1. Verify that the Hand-Off-Auto (HOA) switch on the RO Control Panel is off.
2. Confirm the storage tank is ready to receive water and the drains are all clear.
3. Check to ensure there are no repairs or service in progress to the RO unit or down stream equipment.
4. Verify that the valves on the RO unit are set up correctly.
5. Verify the pre treatment equipment is on-line and ready to supply the RO unit.
6. Test the water quality (TDS, chlorine, temperature, pH) to verify it is within the limits of the membrane elements. Refer to membrane literature in appendix if necessary.
7. If the RO membranes were not installed at the factory, they need to be installed now, before proceeding with the start up. Refer to Section 5.3 for loading instructions.
PRE-START, LOW PRESSURE SYSTEM FLUSHING
New RO membrane elements are shipped with a chemical preservative applied
CAUTION
to the membranes. It is hazardous to your health and will contaminate product water supplies. It must be flushed from the membranes prior to using the RO product water.
1. Verify that the feed water pressure to the RO unit is within 20 to 95 PSIG. If there is no feed pressure, make sure the main supply valve is opened. (If the pressure is too low, you may need to install a feed water booster pump to avoid low pressure fault shutdowns. If the pressure is too high, you must install an automatic pressure regulating valve to
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OPERATION FLOWMAX RO MANUAL REV: B 05/1999
protect the low pressure pump seals and PVC piping from over pressurization.)
2. If applicable, fully open the manual product divert to drain valve. Verify there is no obstruction of this valve. If the automatic divert valves were installed, they will automatically divert to drain when the system is off.
3. Close the air supply valve going to the solenoid valves.
4. Verify that the manual feed water valve (V-1) is fully closed.
5. Fully open the reject valves (V-7 & 8).
6. Manually override the RO unit automatic feed water valve and open this valve. This will allow the RO unit to flush while the power is off. This can be done by applying an air supply directly to the valve actuator.
CAUTION
Always open the manual valves slowly to prevent water hammer from damaging the piping and components.
7. Remove the Lock-out/Tag-out equipment from the manual feed water isolation valve (V-
1). Slowly open the valve to allow water flow into the RO unit.
8. Verify flow through the unit by checking the feed inlet pressure gauge on the wet instrument panel. Check for water flow out of the reject drain line.
9. Allow the flushing process to run for a minimum of 15-30 minutes. This will assure all the membrane preservatives will be flushed out.
10. When flushing is complete, re-connect the air lines and return the valves to the operating position.
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SECTION 4-3
OPERATION FLOWMAX RO MANUAL REV: B 05/1999
4.2 NORMAL OPERATION
Use this section for daily startup or to restart the system after a short term shutdown.
1. BEFORE starting the RO unit, verify that the following conditions exist:
DEVICE CONDITION
RO system H-O-A switch (HAND-OFF-AUTO) OFF
Starter Panel disconnect switch (MCP) ON
Control Panel circuit breaker (inside Control Panel) ON
Control Panel GFCI circuit breaker (for instrumentation) ON
manual feed water isolation valve (V-1) OPEN
instrument isolation air valve OPEN
flush mode selector switch (MANUAL-OFF-AUTO) AUTO
pump discharge throttling valve 1/8 to 1/4 OPEN
reject globe valve open 4 full turns
reject bypass ball valve 1/8 to 1/4 OPEN
any valves in the reject to drain line OPEN
any valves in the process supply line open
manual product divert valve closed
pre treatment equipment ready for use
post treatment equipment ready for use
storage tank ready for use
IF ALL THE ABOVE CONDITIONS EXIST, THE SYSTEM IS READY TO START. CLOSE AND LATCH THE CONTROL PANEL DOOR BEFORE STARTING THE RO UNIT. IF ONE OF THE SETTINGS IS INCORRECT, CORRECT THE SETTING PRIOR TO PROCEEDING.
2. Turn the H-O-A switch to the AUTO position. This will start the system.
NOTE: The pump will not start for 60 seconds. When you turn the H-O-A switch to AUTO, the
feed inlet valves opens to fill the unit with water under low pressure. This purges any air out of the unit. (If any leaks are noticed at this time, turn off the system and correct the leaking component before the pump starts.) After the 60 second delay, the pump will start. Be prepared to adjust the pump discharge and reject valves to correctly set the product and reject flow. If the system does not start up after the initial 60 second delay, check the storage tank. If it is full, the system will not start until the tank drops below the setup point by the tank level sensing device. If the low feed pressure light is on, the system also will not start.
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SECTION 4-4
OPERATION FLOWMAX RO MANUAL REV: B 05/1999
The RO unit should never be run in the HAND mode unless it will be continuously attended by a service technician. Operation in this mode over
CAUTION
rides the automatic shutdown signal provided by the RO product water storage tank level sensing device. This can cause the tank to over fill, causing possible damage to the storage tank or damage to surrounding equipment.
3. Verify that the product and reject flows are correct. If not, adjust the pump discharge throttling valve and the reject valves until the correct parameters are reached. Adjustment procedure:
First, adjust the unit to make the correct amount of RO product water by adjusting the system pressure. This can be accomplished by regulating the pump discharge throttling valve. Further OPEN the valve to increase the system operating pressure and productivity, further CLOSE the valve to reduce the system operating pressure and productivity. Once this flow is correct, make a note of the operating pressure.
Second, adjust the unit to make the correct amount of reject to drain flow by adjusting the reject throttling valves. Control the majority of the flow with the ball valve and fine tune with the globe valve. OPEN the valves to obtain a higher flow rate or CLOSE the valves to reduce the flow rate.
NOTE: This is some what of a "balancing act", in that as you close the reject valves, the product
flow increases and the reject flow decreases. As you open the pump discharge throttling valve, the product and the reject flow increase. You may have to adjust the pump discharge throttling valve to reestablish the operating pressure to obtain the correct product flow as established in the first step.
4. Once the RO unit is operating at the parameters outlined on the RO Operating Specification Sheet in Section 6.2, record the operating parameters on the data collection form. (A sample form is in Section 6.1.) It is imperative to record the operating parameters daily, since RO trouble shooting may require a trended analysis of the RO operating parameters.
NOTE: If the RO will not start, or can not achieve the correct flows, go to the trouble shooting
section for more information.
5. If the RO unit shuts down due to a fault condition, you must turn the HOA switch to OFF, then back to AUTO (or HAND) to reset the Control Panel.
4.3 SHORT TERM SHUTDOWN PROCEDURE
NOTE
:
There are two methods for shutting the RO unit down.
Short term shut down is for when the system will be down for a short period of time, as to perform brief maintenance or service.
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Long term shut down should be used for when the system will be down for a prolonged shutdown, as for major repairs, modifications or going out of service.
1. Turn the H-O-A switch to OFF. Install a Lock Out device and a Lock Out Tag on the switch.
2. Close the manual feed water inlet valve (V-1), located off the RO unit.
3. Once the feed water inlet pressure indicator reads zero, it is safe to service the unit.
The system is now isolated from the standpoint of electrical and hydraulic energy and can now be safely serviced. To restart system, simply open the manual feed water valve and turn the HOA switch back to AUTO.
4.4 LONG TERM SHUTDOWN PROCEDURE
If the system is to be down for a period longer than 7 days, it is recommended that a biocide be pumped into the membrane elements to prevent biological growth. Prior to shutting down the system, read and perform the procedure in Section 5.6, RO Membrane Element Long Term Storage Procedure.
CAUTION
irreversible damage to the membranes due to bacterial growth.
1. Turn the RO unit H-O-A switch and the disconnect switch to the OFF position.
2. Install a Lock-Out device and a lock Out Tag on the disconnect switch.
3. If the RO membranes are to be left in the vessels, go to Section 5.6 Membrane Element Long Term Storage Procedure and follow the instructions there.
4. Fully close the manual feed water isolation valve and install a Lock-Out device and a lock Out Tag on the valve.
5. If applicable, you may also have to fully close any process valves located in the RO unit product line down stream of the product divert to drain valve junction to prevent unwanted RO product water from passing this point, and install Lock-Out / Tag-Out equipment on the valve.
The RO UNIT is now isolated from a standpoint of electrical energy and hydraulic or water pressure energy and may be safely stored for up to a year. If longer storage is required, the membranes need to be removed and stored under more controlled conditions. Contact U.S. Filter for more details.
Failure to store the membranes in a biocide for long term shutdown can cause
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OPERATION FLOWMAX RO MANUAL REV: B 05/1999
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SECTION 5-1
MAINTENANCE FLOWMAX RO MANUAL REV: B 05/1999
5.0 MAINTENANCE
5.1 MAINTENANCE SCHEDULE
PROCEDURE FREQUENCY
Check system for leaks and failures Daily Check feedwater chlorine levels Daily Collect operational data and adjust valves to achieve proper flow rates Change prefilter cartridge elements monthly or when the pressure differential reaches 10-15
Test GFCI monthly Lubricate pump motor bearings 2 times a year Calibrate instrumentation 2 times a year Clean RO membrane elements When normalized productivity rate drops by more than
Replace RO membrane elements When cleaning the membranes fails to restore the proper
*
Contact U.S. Filter for replacement.
Daily
PSIG, which ever occurs first
15% of the clean membrane normalized productivity rate, when the RO feed pressure increases by 25 PSIG over the clean feed pressure, or when the RO rejection rate drops by more than 3%
performance *
5.2 FILTER CARTRIDGE REPLACEMENT (IF APPLICABLE)
Required down time: 25 minutes
The following is required:
replacement filter cartridges adjustable wrench
1. Shut down RO unit as described in Section 4.3.
2. Wait until the automatic feed water valve fully closes, as evidenced by the feed inlet pressure indicator winding down to 0 (zero).
3. Open the vent valve on top of the filter housing to relieve any pressure, then remove the top of the filter housing by loosening the swing bolts.
4. Drain the water in the filter housing by opening the drain valve.
5. Remove the old filter cartridge elements and dispose of them.
6. Rinse the filter housing out with fresh water.
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MAINTENANCE FLOWMAX RO MANUAL REV: B 05/1999
7. Install the new filter elements by setting them over the holes in the bottom of the filter housing. Place the tension springs over the holes on top the new elements.
8. Replace the top of the filter housing and tighten down the swing bolts.
9. Restart system as described in Section 3.2, and check for leaks around the top o-ring seal.
10. If no leaks are observed, the RO unit is back in normal service.
11. If a leak is detected, turn the RO unit off, wait for the automatic feed water valve to fully close, remove the top, and inspect the o-ring for damage. If damage is observed, replace the o-ring.
5.3 MEMBRANE ELEMENT REPLACEMENT
Required down time: 2 - 6 hours
You will need the following:
safety equipment (glasses, boots, etc.) Lock-Out / Tag-Out equipment rubber mallet 24 liquid ounces of glycerin set of new membrane elements
1. Secure the unit for a short term shutdown as described in Section 4.3
2. Remove the product pipe connection from the end of the pressure vessel by un-screwing the PVC union in the product lines. Some water will inevitably drain from the broken plumbing connections so be prepared for a wet floor.
NOTE: The flow arrowhead sticker located on one end of the pressure vessel indicates the
direction of flow through the pressure vessel. You must unload and reload the new RO membrane elements in the direction of flow. This greatly reduces the chance of rolling or damaging the brine seals.
3. To determine the correct procedure for pressure vessel end cap disassembly, consult the pressure vessel manufacturers literature in the Appendix.
4. Remove the retaining rings that hold the end caps.
5. Carefully remove the end caps by applying even steady pulling force on them.
NOTE: Be sure to make note of which end cap came out of which end of the pressure vessel so
they may be reinstalled in the same vessels.
6. Push the old membrane elements out of the pressure vessel in the direction of the flow
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arrowhead sticker on the outside of the vessel.
7. Remove the membrane product tube adapters from the old membrane elements if they did not remain on the vessel end caps and keep them. Dispose of the old membrane elements.
8. Check the o-rings on the interconnectors for damage and replace any that show signs of wear or damage. (It is a good idea to replace all the o-rings at the same time you replace the RO membrane elements). Apply a liberal coating of glycerin to the o-rings and brine seals before they are inserted back into the pressure vessel.
9. Remove enough new RO membrane elements from the protective packaging to fill one pressure vessel.
10. Install the interconnectors between the RO membrane elements as you load them into the vessel.
11. Load the new membrane elements in the pressure vessel in the same direction as the flow arrowhead sticker. Make sure that the membrane brine seal is on the end to enter the pressure vessel last.
NOTE: The flow arrow on the new RO membrane element should match the flow arrowhead
sticker on the pressure vessel.
12. Carefully reinstall the product tube adapters on the ends of the membrane element product tubes. Apply a liberal amount of glycerin on the o-rings to make installation easier.
13. Carefully reinstall the end caps back in the ends of the pressure vessel, taking care to put them in the same ends that they came out of. Use a small amount of glycerin on the o­rings to make installation easier.
14. Carefully tap the end caps into place, using the rubber mallet. Re-assemble the end cap assembly per manufactures instructions.
15. Carefully reinstall the retaining rings in both ends of the pressure vessel.
16. Once all the membranes are replaced, reinstall the product piping connections.
17. Check all connections and vessels carefully.
The RO unit is now ready to be put back into service.
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SECTION 5-4
MAINTENANCE FLOWMAX RO MANUAL REV: B 05/1999
5.4 TROUBLESHOOTING
PROBLEM: CONTROL POWER IS OFF
CAUSE ACTION
Power source disconnect is opened or fuses
Check the power source and fuses. have blown. RO unit Control Panel fuses may be blown. Check the fuses and replace them if necessary. RO unit Control Panel low voltage circuit breaker may be tripped.
Check the Control Panel low voltage circuit breaker
and reset it if necessary.
PROBLEM: RO UNIT WILL NOT START IN THE HAND MODE
CAUSE ACTION
The RO unit pre-treatment interlock may be engaged because of a filter backwash or a softener regeneration cycle.
Check the operational status of the pre-treatment system. Check out the Control Panel circuitry to ensure the
proper jumpers have been installed. Low feed pressure fault may have caused the RO unit to drop out of service.
Turn the RO unit H-O-A switch to the OFF position
and then to the AUTO position. Allow the RO unit to
restart, and check that the feed pressure is at least 10
PSIG. The RO unit Control Panel motor overload may have tripped.
Reset the motor overload and observe the operation of
the RO unit to determine if this was a transient trip or
if there is a more serious electrical problem. The RO unit Control Panel may have an
Inspect all components of the Control Panel. electrical component failure.
PROBLEM: RO UNIT WILL NOT START IN THE AUTO MODE
CAUSE ACTION
The RO unit pretreatment interlock may be engaged because of a filter backwash or a softener regeneration cycle.
Check the operational status of the pretreatment system. Check out the Control Panel circuitry to ensure the proper jumpers have been installed.
The RO water storage tank may be full. No action is required. unit is in standby mode, storage
tank full indicator should be on. The RO water storage tank level sensing device may be broken or require adjustment.
Inspect the electrical functioning of the RO water
storage tank level sensing device. Inspect the settings
of the RO water storage tank level sensing device.
PROBLEM: AUTOMATIC FEED WATER VALVE WILL NOT OPEN
CAUSE ACTION
Solenoid valve may have failed. Replace the solenoid valve. Feed water valve actuator may have failed. Repair or replace the actuator.
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SECTION 5-5
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PROBLEM: RO UNIT PRODUCTIVITY IS LOW
CAUSE ACTION
RO unit operating pressure is too low. Readjust the RO unit operating pressure. RO unit product back pressure is excessive. Check the pressure of the RO unit product plumbing,
it should not exceed 25 PSIG. If it does, determine
what is causing the pressure drop and reduce it. RO unit feed water temperature is colder then usual. (Lower feed water temperatures require a higher operating pressure.)
Check the RO unit feed temperature. If it has
decreased, increase the operating pressure to
compensate for this low temperature operation. RO unit membrane elements may be fouled. Determine the nature of the foulant and clean and/or
sanitize the membrane elements. Flowmeter readings not accurate. Verify correct operation of flow sensors and flow
meters. Calibrate or replace if necessary. RO pretreatment failure. Inspect all pretreatment systems for problems.
PROBLEM: RO UNIT REJECTION IS LOW
CAUSE ACTION
Inadequate operating pressure. Increase RO unit operating pressure by further
opening pump discharge valve. RO unit recovery is too high. Reduce RO unit recovery to match values listed in
RO operating spec sheet in the Appendix. Shift in feed water chemistry (oxidants in feed water).
Check feed water chemistry. If substantially different
from the original design feed water chemistry, have a
new RO performance projection run to determine
what the rejection rate characteristic should be. Mechanical leak in the membrane system. Inspect all RO product tube adapter o-ring seals. RO feed water temperature increase. Check feed water temperature. Install or adjust
temperature controls, if necessary. RO unit reject to waste flow out of adjustment. Check flow parameters and adjust system as stated in
Section 3.2 RO unit membrane elements may be fouled. Determine the nature of the foulant and clean and/or
sanitize the membrane elements.
PROBLEM: CAN NOT ACHIEVE PROPER FLOW READINGS
CAUSE ACTION
Flow Sensors not operating correctly. Verify proper calibration of the flow sensors.
Flow monitoring devices may have failed. Confirm operation of digital flow monitors. Replace
Control valves not properly adjusted. Reset the control valves as stated in Section 3.2. Control valve may have failed. Check that there are no obstructions or damage to the
5.5 RECOMMENDED SPARE PARTS
USFilter United States Filter Corporation
Replace or re-calibrate as required.
if necessary. Refer to Literature in Appendix for
detailed trouble shooting of this component.
control valves. Check seats on ball valves for
excessive wear.
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SECTION 5-6
MAINTENANCE FLOWMAX RO MANUAL REV: B 05/1999
The following spare parts list includes spare parts of three different priority levels:
Priority A Parts: Includes the bare minimum of spare parts and consumables that U.S. Filter
recommends to every customer.
Priority B Parts: Includes spare parts that have a tendency to need replacement within a five year
period. Failure of most of these items would cause an unscheduled shutdown.
Priority C Parts: U.S. Filter recommends these items for customers who foresee difficulty in
obtaining spare parts in a timely manner. Also for customers who cannot shutdown for more than a 24 hour period.
Refer to your unit for specific part numbers for these components, this Manual covers all 20 models.
PRIORITY A PARTS: QTY
Control Panel indicator light bulbs 6 Filter elements A/R* Flow sensor 1 Flow monitor 1 Sodium bisulfite (food grade) A/R Lubricating glycerin A/R Propylene Glycol or Glycerol (for freeze protection only) A/R set of membranes o-rings and brine seals 1 set *A/R stands for as required by your unit.
PRIORITY B PARTS: QTY
Conductivity sensor 1 Solenoid valve 1 10 amp circuit breaker 1 15 amp GFCI circuit breaker 1 Automatic reject bypass valve 1 Automatic feed valve 1
RO Membrane Element(s)* 1 Set RO High Pressure Pump 1
*
Membranes have a shelf life of only a year.
USFilter United States Filter Corporation
PRIORITY C PARTS: QTY
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SECTION 5-7
MAINTENANCE FLOWMAX RO MANUAL REV: B 05/1999
5.6 RO MEMBRANE ELEMENT LONG TERM STORAGE PROCEDURE
The solution USFilter recommends is a 0.5 to 1.0% solution of sodium bisulfite. For conditions where freezing may be a problem, the solution should also contain up to 18% (by weight) glycerin or propylene glycol. Refer to RO membrane data sheet in Appendix for further information.
The following equipment and materials are needed:
USFilter CIP Cleaning Skid RO Product Water or DI Water Sodium Bisulfite (food grade) Propylene Glycol or Glycerin (if required) Safety Equipment
1. Fill the tank on the cleaning skid with the appropriate quantity of RO product water or DI water.
CAUTION
Do not use a solution of greater than 1.0%. The pressure vessel endcaps will be damaged otherwise.
2. Add the correct amount of sodium bisulfite powder to the cleaning tank using the following proportions:
0.5% solution sodium bisulfite - .042 lbs. per gallon
1.0% solution sodium bisulfite - .084 lbs. per gallon
If applicable, add the appropriate amount of freeze protection (glycerin or propylene glycol) to the solution at this point. (Refer to Table 1 & 2 at the end of this Section)
3. Adjust the valves on the cleaning skid to the recirculation position.
4. Run the cleaning skid for at least 5 minutes to allow for complete mixing.
5. Close the RO pump discharge throttling valve.
6. Connect the supply hose from the cleaning skid to the cleaning port on the first stage feed manifold.
7. Connect hoses from the RO unit product and reject outlets back to the cleaning tank.
8. Close the proper valves on the product and reject lines to prevent solution from entering the storage tank.
9. Fully open the RO unit reject valves.
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10. Reset the valves on the cleaning skid to the normal position.
11. Start the cleaning skid pump.
12. Allow the solution to circulate through the RO unit for 30 minutes.
13. Turn off the cleaning skid and disconnect the hoses.
14. Fully close the manual feed water isolation valve and install a Lock-Out device and a Lock Out Tag on the valve.
15. Fully open the product divert to drain valve and install a Lock-Out device and a Lock Out Tag on the valve.
16. If applicable, you may also have to fully close any process valves located in the RO unit product line down stream of the product divert to drain valve junction to prevent unwanted RO product water from passing this point, and install a Lock-Out device and a Lock Out Tag on the valve.
17. Drain the pump and manifold piping.
18. Seal all openings to prevent the membrane elements from drying out.
19. Tag the RO unit with the date and type of solution the membranes are stored in so that it is properly flushed prior to being put back into service.
The RO unit is now ready to be stored. Be sure to follow the Initial Startup in Section 4.1 when ready to put the unit back in service.
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Table 1
FREEZING POINT OF PROPYLENE GLYCOL - WATER MIXTURES
% glycol by
VOLUME
Specific Gravity
15.6oC. (60oF)
Freezing Point oC. Freezing Point oF.
5 1.004 -1.1 30 10 1.006 -2.2 28 15 1.012 -3.9 25 20 1.017 -6.7 20 25 1.020 -8.9 16 30 1.024 -12.8 9 35 1.028 -16.1 3 40 1.032 -20.6 -5 45 1.037 -26.7 -16 50 1.040 -33.3 -28
Table 2
FREEZING POINT OF GLYCEROL (GLYCERIN) - WATER MIXTURES
% glycerin by
WEIGHT
Specific Gravity
15.0oC. (59oF)
Freezing Point oC. Freezing Point oF.
10 1.02415 -1.6 29.1 20 1.04935 -4.8 23.4 30 1.07560 -9.5 14.9 40 1.10255 -15.5 4.3 50 1.12985 -22.0 -7.4 60 1.15770 -33.6 -28.5 70 1.18540 -37.8 -36.0 80 1.21290 -19.2 -2.3 90 1.23950 -1.6 29.1
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SECTION 5-10
MAINTENANCE FLOWMAX RO MANUAL REV: B 05/1999
5.7 RO MEMBRANE ELEMENT CLEANING
NOTE: To clean the membrane elements in situ, a CIP skid (stands for Clean I
n Place) is required. This can be purchased from USFilter if you want to do your own cleaning. Cleaning services are available from the most of the USFilter service branches. Call the local sales and service office for details.
Read the following section to help you understand why RO membrane elements need to be cleaned, and the nature of the foulants that can be encountered.
NOTE: RO membrane element cleaning is a complex process and if done incorrectly, could
destroy the membrane elements. A complete cleaning procedure is described in the CIP operating manual.
It should be noted that a decrease in water temperature will result in a decrease in product water flow and increase in the differential pressure across the membrane. This is not indicative of a requirement for cleaning.
The data collected after the first 24 to 48 hours of operation of the RO unit should be used as a baseline for the above parameters. It is critical that the data collection sheets, supplied in the Appendix, are completely filled out on a daily basis.
You will find it necessary to clean the RO UNIT from time to time as a result of the natural accumulation of some type of membrane surface foulant. This requirement to clean the RO UNIT membranes will be evidenced by one or more of the following symptoms including, a reduction in the NORMALIZED PRODUCTIVITY RATE, a reduction in the RO UNIT TOTAL DISSOLVED SOLIDS REJECTION RATE, or an increase in the RO UNIT OPERATING PRESSURE, in spite of no change in the RO UNIT feed water temperature. In general, this procedure should not be required more then three (3) times per year or about every four (4) months. If you find that this procedure is required more frequently then this, you should have a U.S. Filter representative evaluate the effectiveness of your pre-treatment system or the current RO UNIT operating parameters. Most cleaning procedures consist of the preparation of a specific cleaning chemical formulation made up in warm water, which is then recirculated through the RO UNIT elements, followed by an extended soak period in the cleaning solution, followed by another recirculation cycle, and completed with a thorough rinse cycle.
The RO UNIT membrane foulants usually consist of one or more of three common classes of foulants including; SUSPENDED SOLIDS, ORGANIC FOULANTS AND PRECIPITATED DISSOLVED SOLIDS. A brief explanation of the nature of each type of foulant will is below.
SUSPENDED SOLIDS FOULANTS
Suspended solids fouling is among the most common RO UNIT foulants. This fouling condition results from the incomplete removal of suspended solids such as silt and clay particles from the RO UNIT feed water. In as much as some of these particles are less then 0.2 micron in size, it is not practical to attempt to remove all of them so this type of membrane fouling is eventually inevitable in all RO UNITS. This is most common to systems operating on a surface water supply. The trick is to try to eliminate as much of the suspended solids material as possible,
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MAINTENANCE FLOWMAX RO MANUAL REV: B 05/1999
through good pre-treatment filtration practices including, proper selection and operation of multimedia filtration, the correct selection and maintenance of cartridge filters, and the possible use of chemicals aimed at dispersion of suspended solids. This type of foulant is generally evidenced by a gradual reduction in the NORMALIZED PRODUCTIVITY RATE with no reduction in the TOTAL DISSOLVED SOLIDS REJECTION RATE.
ORGANIC FOULANTS
Organic fouling of thin film composite membranes is very common and may take place as a result of two different mechanisms. The first mechanism may be through the presence of organic material present in the RO UNIT feed water in the form of humic or fulvic acids, which end up in the water supply as a result of rotting vegetation. Obviously this is more of a problem when using surface water supplies as opposed to well water supplies.
The second mechanism is the result of actual biological growth taking place on the membrane surface as a result of the lack of an oxidant in the RO UNIT feed water to kill off these microorganisms. It is usually impractical to totally eliminate all organic foulants from the RO UNIT feed water, so all you can do is try to take reasonable precautions through the possible use of ultraviolet sterilizers on the RO UNIT feed water, conduct good maintenance procedures on the multimedia filters, including periodic sterilization cycles, and the use of approved biocides on the RO UNIT MEMBRANE ELEMENTS. This type of foulant is evidenced by a gradual
reduction in the NORMALIZED PRODUCTIVITY RATE with either no reduction or a slight increase in the TOTAL DISSOLVED SOLIDS REJECTION RATE.
PRECIPITATED DISSOLVED SOLIDS FOULANTS
Precipitated dissolved solids fouling is generally the least common foulant to plague RO UNIT membranes. This type of fouling generally occurs when the RO UNIT recovery is run too high, thus concentrating the dissolved solids in the feed water to the last few membranes beyond their solubility limits. The most common constituents of this type of foulant are Silica (SiO2), Calcium Carbonate (CaCO3), Calcium Sulfate (CaSO4) and various forms of Iron (Fe) and Aluminum (Al). Generally this type of fouling is preventable through good administrative control of RO UNIT recovery, and maintenance of pre-treatment equipment including ion exchange softeners and antiscalant injection systems. This type of foulant is evidenced by a gradual reduction in NORMALIZED PRODUCTIVITY RATE with a minor reduction in the TOTAL DISSOLVED SOLIDS REJECTION RATE.
Refer to the manual included with the optional CIP skid for complete cleaning instructions.
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SECTION 6-1
APPENDIX FLOWMAX RO MANUAL REV: B 05/1999
6.0 APPENDIX
6.1 RO DATA COLLECTION FORM
SYSTEM IDENTIFICATION: _________________________________________________________
WEEK ENDING DATE: ______________________________________________________________
See calculated values on next page.
RO UNIT OPERATING PARAMETERS S M T W T F S
RO Cartridge Filter Pressure Drop (PSI)
RO Cartridge Filter Outlet Pressure (PSI)
RO Cartridge Filter Inlet Pressure (PSI)
Feed Flow Rate (GPM)
2
Product Flow Rate (GPM)
Reject Flow Rate (GPM)
Reject Recirculation Flow Rate* (GPM)
Product Recovery (%)
3
Feed Water Temperature (oF)
Feed Water pH (0-14)
Feed Water Chlorine Concentration (PPM)
Feed Water Total Hardness (PPM)
Feed Water SiO2 (PPM as SiO2)
Feed Water Conductivity (mg/l)
rst
RO 1
Stage Conductivity (PSI)
RO 2nd Stage Conductivity (mg/l)
RO 3rd Stage Conductivity (mg/l)
RO Final Reject Conductivity (mg/l)
RO Percent Rejection (%)
rst
RO 1
Stage Operating Pressure (PSI)
4
RO 2nd Stage Operating Pressure (PSI)
RO 3rd Stage Operating Pressure (PSI)
RO Final Reject Operating Pressure (PSI)
RO Normalized Productivity (GPM)
DATA TAKEN BY:
* 3M units only
COMMENTS:
1
5
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SECTION 6-2
APPENDIX FLOWMAX RO MANUAL REV: B 05/1999
Calculated Values:
1: RO FILTER PRESSURE DROP is equal to filter inlet pressure MINUS filter outlet pressure.
2: RO FEED FLOW rate is equal to RO product flow PLUS the RO reject flow.
3: RO PRODUCT RECOVERY is equal to the RO product flow rate DIVIDED by the RO feed
flow rate, MULTIPLIED by 100.
EXAMPLE: Product flow = 30 GPM
Feed flow = 40 GPM (30 ÷ 40) x 100 = 75% recovery
4: RO PERCENT REJECTION* is equal to the RO feed conductivity MINUS the RO product
conductivity, DIVIDED by the feed conductivity, TIMES 100.
EXAMPLE: Feed conductivity = 380 micromoh
Product conductivity = 5 micromoh {(380-5) ÷ 380} x 100 = 98.6% rejection
* the RO Quality monitor is set up at the factory to display this value.
5: NORMALIZED PRODUCTIVITY is a true indication of membrane performance. It is
calculated as follows:
NPF = MPF X TCF X (225÷MFP)
Where:
NPF = NORMALIZED PRODUCTIVITY FLOW MPF = MEASURED PRODUCT FLOW TCF = TEMPERATURE CORRECTION FACTOR (See table next page) MFP = MEASURED FEED PRESSURE
EXAMPLE: MPF = 35 GPM
FEED WATER TEMP = 60 oF, THEN TCF = 1.44 MFP = 285 PSIG
NPF = 35 x 1.44 x (225÷285) NPF = 35 x 1.44 x .789 NPF = 39.8
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RO FEED WATER TEMPERATURE CORRECTION FACTOR
TEMP oF TCF TEMP oFTCF
34 3.64 70 1.12
36 3.18 72 1.08
38 2.93 74 1.05
40 2.68 76 1.02
42 2.47 78 0.97
44 2.29 80 0.93
46 2.14 82 0.90
48 2.01 84 0.88
50 1.88 86 0.86
52 1.77 88 0.82
54 1.68 90 0.79
56 1.59 92 0.77
58 1.51 94 0.75
60 1.44 96 0.73
62 1.36 98 0.70
64 1.30 100 0.68
66 1.24 102 0.65
68 1.17 104 0.63
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APPENDIX FLOWMAX RO MANUAL REV: B 05/1999
6.2 RO OPERATING SPECIFICATION SHEET
ALL FLOW RATES EXPRESSED AS GALLONS PER MINUTE (GPM). OPERATING AT DIFFERENT GFD RATINGS WILL PROVIDE DIFFERENT FLOW RATES, HOWEVER THIS UNIT IS DESIGNED TO OPERATE AT 16.5 GFD, OPERATING OUTSIDE THESE FLOWS IS NOT RECOMMENDED WITOUT CONSULTING U.S. FILTER
BW30-365 membranes
GFD GFD GFD GFD GFD
ARRAY QTY
3M 1:1:1 9 35 37 40 42 44 3M 2:1:1 12 47 50 53 56 59 3M 3:2:1 18 70 75 80 84 89
4M 3:2:1 24 94 100 106 113 118 4M 4:2:1 28 109 115 124 131 138 4M 5:3:2 40 156 165 177 188 197
6M 5:3 48 188 200 212 225 237 6M 6:3 54 211 225 239 253 266 6M 6:4 60 235 250 265 281 296 6M 8:4 72 282 300 318 338 355
The recommended flux rate for maximum membrane life
15.5 16.5 17.5 18.5 19.5
should not exceed 16.5 GFD
NOTE:
VALUES LISTED ABOVE ARE NOMINAL FLOW RATES BASED ON AVERAGE FEED WATER CONDITIONS. A CHANGE IN WATER TEMPERATURE AND OR WATER QUALITY CAN SIGNIFICANTLY ALTER THE ACHIEVABLE FLOW RATES OF THE RO SYSTEM.
TO OBTAIN OPTIMAL OPERATING PARAMETERS FOR YOUR SYSTEM, BASED ON YOUR FEED WATER CONDITIONS, PLEASE SUBMIT A WATER ANALYSIS OF YOUR FEED WATER TO THE U.S. FILTER ENGINEERING DEPARTMENT, AND WE WILL RUN A COMPUTERIZED RO PROJECTION FOR YOUR SYSTEM.
OPERATING THE RO UNIT OUTSIDE OF THESE PARAMETERS COULD CAUSE PREMATURE MEMBRANE FAILURE OR RESULT IN ECSESSIVE CLEANING REQUIREMENTS.
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6.3 QA DATA SHEETS
See QA Data sheet that follows this page.
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6.4 DRAWINGS
There are 20 different models of the FlowMAX RO unit. Only the drawings checked below that apply to your system will be included in this section.
DWG # Model DESCRIPTION
S8600-001 ALL MAX RO BLOCK FLOW DIAGRAM S8600-012 ALL FLOWMAX HORIZONTAL P&ID
S8601-020 FM3-09 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-021 FM3-12 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-022 FM3-18 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-023 FM4-24 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-024 FM4-28 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-025 FM4-40 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-026 FM6-48 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-027 FM6-54 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-028 FM6-60 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-029 FM6-72 PACKAGED SYSTEM EQUIP SPEC DRAWING
S8601-030 FS3-09 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-031 FS3-12 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-032 FS3-18 PACKAGED SYSTEM EQUIP SPEC DRAWING
S8601-033 FS4-24 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-034 FS4-28 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-035 FS4-40 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-036 FS6-48 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-037 FS6-54 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-038 FS6-60 PACKAGED SYSTEM EQUIP SPEC DRAWING S8601-039 FS6-72 PACKAGED SYSTEM EQUIP SPEC DRAWING
ELECTRICAL DOCUMENTATION
S8693-050 ALL FIXED I/O PANEL SCHEMATIC S8693-999 ALL PLC LADDER LOGIC FOR FIXED I/O PANEL
SCHEMATIC
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6.5 COMPONENT MANUFACTURERS LITERATURE
Component Manufacturer Model Number Included*
Pump Horizontal T&T H Series Pump Submersible Grundfos BM Series Pressure Vessels Advanced Structures 80A Series RO Membranes Filmtec BW30-365 RO Membranes Filmtec BW30-400 RO Membranes Filmtec BW30-440LE % Rejection Monitor Thornton 200CR PLC Micrologix Allen Bradley 1000 Flow Sensor Fluidyne 2300 Flow Monitor Thornton 200F pH Monitor (optional) Thornton 200pH
*Only the literature that applies to your system will be included in this section.
6.6 MATERIAL SAFETY DATA SHEET(S)
Title Use
Sodium Bisulfite RO membrane preservative
USFilter United States Filter Corporation
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