Monitoring for Negative and Transient Pressures in Distribution Mains

Similar documents
Monitoring for Transient Pressures in Pipelines. By Will Worthington, P.E. 1

Journal of Applied Fluid Transients, Vol 1-1, April 2014 (3-1)

PROVING THAT BLADDER SURGE TANKS CURED EXCESSIVE SURGE CONDITIONS IN A 30 FORCE MAIN

MITIGATING PIPE AND RISER HYDRAULIC PIPELINE ISSUES WITH THE I-RISER PLUS

The Future of Hydraulic Control in Water-Systems

Pumping Systems for Landscaping Pumps, Controls and Accessories. Mark Snyder, PE

PRESSURE SURGES IN PIPELINES

Susceptibility of Distribution Systems to Negative Pressure Transients. Presenters: Kala Fleming and Mark Le Chevallier Moderator: Jian Zhang

Appendix M. Hydraulic Transient Analysis

SECTION PRESSURE TESTING OF PIPING

Tirpur Area Water Supply Project A Report on Transient Modeling Study

Courses of Instruction: Controlling and Monitoring of Pipelines

Training Fees 4,000 US$ per participant for Public Training includes Materials/Handouts, tea/coffee breaks, refreshments & Buffet Lunch.

Sizing Pulsation Dampeners Is Critical to Effectiveness

Installation and operation Manual. Bermad Surge Anticipation Valve. Model No 435

CONTROL VALVE TESTING

OWNER S TECHNICAL MANUAL

IT STARTS AT THE SOURCE - RE-CALIBRATING YOUR PLANT METERS

FIRE PROTECTION. In fact, hydraulic modeling allows for infinite what if scenarios including:

Engineering / Technical Section

The Protection of Silos From Over. Pressurisation During Filling

EVT * -Pro Electronic Valve Tester

Intelligent SUNTEX DC-5310(RS) Dissolved Oxygen Transmitter

3. REQUIRED EQUIPMENT

Effect of noise in the performance of the transducers in an ultrasonic flow meter of natural gas

2600T Series Pressure Transmitters Plugged Impulse Line Detection Diagnostic. Pressure Measurement Engineered solutions for all applications

Every things under control High-Integrity Pressure Protection System (HIPPS)

BACK PRESSURE / SUSTAINING

JUST WHEN YOU HAD SEEN IT ALL: THE VALUE OF HIGH FREQUENCY PRESSURE DATA. James Dunning, CEO tel:

TECHNICAL DATA Q= C. Table 1 - Specifications

BLOCKAGE LOCATION THE PULSE METHOD

BACK PRESSURE / SUSTAINING

SIL explained. Understanding the use of valve actuators in SIL rated safety instrumented systems ACTUATION

SEMATECH Provisional Test Method for Pressure Cycle Testing Filter Cartridges Used in UPW Distribution Systems

Inflatable Packers for Grouting 11/10/00

RESILIENT SEATED BUTTERFLY VALVES FUNCTIONAL SAFETY MANUAL

Double whammy: the benefits of valve signatures and partial stroke testing

SINGER MODEL 106/206-RPS-L&H

TECHNICAL DATA. the Viking Pilot Pressure Regulating Valve 1 Model A-1 Speed Control Assembly: OBSOLETE. the Viking Speed Control Assembly 1

BUTTERFLY VALVES Series 800

Pressure management for Large

Understanding the How, Why, and What of a Safety Integrity Level (SIL)

DF1 and DF2 Diffusers

UNIT 15 WATER HAMMER AND SURGE TANKS

Multiple Pressure Booster Systems With Variable Speed Controller Type BL

TECHNICAL DATA. Table 1 - Specifications

Spirax Compact FREME Flash Recovery Energy Management Equipment

MIL-STD-883G METHOD

Fail Operational Controls for an Independent Metering Valve

TEST BENCH SAFETY VALVES ¼ - 5 DN10 DN125

A SEMI-PRESSURE-DRIVEN APPROACH TO RELIABILITY ASSESSMENT OF WATER DISTRIBUTION NETWORKS

Effect of Pump Inertia & Valve Closure time on the Transient Flow Condition of a Water Supply Network: A Case Study

Model DDX-LP Dry Pipe Valve System 8 (200mm) Features. Differential latching clapper-type, lighweight, dependable construction.

OIL SUPPLY SYSTEMS ABOVE 45kW OUTPUT 4.1 Oil Supply

SECTION 25 TESTING AND DISINFECTING WATER MAINS General

Reliability of Safety-Critical Systems Chapter 3. Failures and Failure Analysis

Discharge Relief Valve Operation & Maint.

LECTURE 3 MAINTENANCE DECISION MAKING STRATEGIES (RELIABILITY CENTERED MAINTENANCE)

Suppress Your Surges: Surge Suppression Fundamentals. April 13, 2017

Exercise 4-2. Centrifugal Pumps EXERCISE OBJECTIVE DISCUSSION OUTLINE DISCUSSION. Pumps

TROUBLESHOOTING GUIDELINES

CHEMICAL ENGINEERING LABORATORY CHEG 239W. Control of a Steam-Heated Mixing Tank with a Pneumatic Process Controller

FUNDAMENTAL SAFETY OVERVIEW VOLUME 2: DESIGN AND SAFETY CHAPTER P: REFERENCE OPERATING CONDITION STUDIES (PCC)

DAV - P. Product Catalogue DAV - P. Air release & Vacuum Break Valves. (Plastic Air Valves) DAV - P. Edition 2012

Section 1: Multiple Choice

BUBBLER CONTROL SYSTEM

SEMS II: BSEE should focus on eliminating human error

M-06 Nitrogen Generator (Nitrogen Making Machine)

The benefits of the extended diagnostics feature. Compact, well-proven, and flexible

Experimental Study of Water Hammer Pressure in a Commercial Pipe

Using LOPA for Other Applications

This session covers the safety procedure known as lockout/tagout, which is required by Occupational Safety and Health Administration (OSHA) in its

Safety. April 2018 Supersedes all previous publications 2018 Chevron Phillips Chemical Company LP

Water Hammer In Irrigation Systems 1

2 FUSION FITTINGS FOR USE WITH POLYETHYLENE PRESSURE PIPES DESIGN FOR DYNAMIC STRESSES

Features. Model DDX-LP Dry Pipe Valve System 4 (100mm), 6 (150mm) & 165mm Sizes

CEPA Initiative: Response Time Guideline 2015 EMERGENCY SECURITY MANAGEMENT WORK GROUP

innova-ve entrepreneurial global 1

Hydraulic transients, also known as pressure

for Building facilities Industrial facilities etc.,multipurpose Pilot operated type(high capacity)

Modelling Today for the Future. Advanced Modelling Control Techniques

BERMAD Fire Protection Hydraulic Control Valves

Effects of Delayed RCP Trip during SBLOCA in PWR

CFD Analysis of the Anti-Surge Effects by Water Hammering

Installation, Operating and Maintenance Instructions. V914 Cast Iron Flanged Swing Check Valve V914

VALVES OPERATION, MAINTENANCE & TROUBLESHOOTING

Cable Pressurization Buffering

System Operating Limit Definition and Exceedance Clarification

Data Sheet Issue A

ZIN Technologies PHi Engineering Support. PHi-RPT CFD Analysis of Large Bubble Mixing. June 26, 2006

Laboratory studies of water column separation

Construction Dewatering

AUTOMATIC HOSE TEST UNIT, TYPE SPU

CASE STUDY. Elvington To Brayton Barff Air valve replacement Program

RESOLUTION A.567(14) adopted on 20 November 1985 REGULATION FOR INERT GAS SYSTEMS ON CHEMICAL TANKERS

Offshore Equipment. Yutaek Seo

Vibration and Pulsation Analysis and Solutions

Questions & Answers About the Operate within Operate within IROLs Standard

Model: 43T. Bermad Pressure Relief Valve

Module 3 Developing Timing Plans for Efficient Intersection Operations During Moderate Traffic Volume Conditions

Transcription:

Monitoring for Negative and Transient Pressures in Distribution Mains Will Worthington, P.E. President Pipeline Technologies Inc. and Pipetech International Carefree, Arizona Abstract Negative pressures and transient pressures may affect water quality and structural integrity of distribution mains. A change in the flow rate in a full distribution main will cause a change in the pressure within that distribution main either positive or negative. Positive transient pressures exceeding the structural strength of the distribution main will cause damage in the form of rupture or, as is more frequently the case, in the form of latent damage that results in failure at a later date. Negative pressures may cause damage in the form of structural collapse of flexible distribution main materials, and waterhammer; and may lead to the intrusion of contaminated groundwater into the water main. Engineers are pretty good at modeling distribution main hydraulics, and at designing to prevent damaging events. On the other hand, it has been difficult to actually measure these pressures after the distribution main is constructed, to determine if the internal transient and negative pressures are consistent with the design. Advances in digital data processing systems have significantly improved our ability to continuously monitor and record negative pressures and even the very-short waterhammer event. These improvements have facilitated monitoring for transient pressures under a wide variety of circumstances. Early detection of damaging transient pressure events is now more practicable, thus permitting the reduction of damage to distribution mains resulting from these events. This paper will briefly describe the causes of transient pressures and improvements in tools available to detect transient pressures. It will conclude with suggestions to civil engineers and distribution main owners regarding what we can do to reduce damages from transient pressures. Background Pipeline and distribution main failures are occasionally traced directly to the occurrence of transient pressures that have caused damage. Among the more familiar ruptures in this category are the failures in Dallas, TX; San Juan, Puerto Rico; Metropolitan Water District of Southern California; Houston, TX, Oigawa Penstock, Japan; and Bartlett Dam, AZ. The last mentioned caused catastrophic rupture at the outlet of the hydro generator, with fatal injuries to the operator. Countless other failures are believed to have resulted from transient pressures, but the evidence is not conclusive. In many cases the transient pressure events occurred repeatedly without detection prior to the failure. 1

Figure 1 Transient-caused failure, Superaqueduct of Puerto Rico A transient pressure in a pipeline is a generic term for a wave phenomenon that accompanies a sudden change of the velocity of the fluid in the pipeline. Authors variously use the term surge pressure to denote a transient pressure that has no detrimental effect, whereas the term waterhammer may be used to denote a transient pressure that will have serious consequences if not properly addressed and mitigated. Pressure transients can be positive or negative. The magnitude of these surges is independent of the operating pressure, and can be many times normal operating pressure. Any event that causes a sudden change in the velocity of fluid in a distribution main will generate a transient pressure. The most common sources of transient pressures are Pump operational on/off cycles Sudden power failure at pumping plants Control valve operation Sudden changes in demand Air release valve operation Pressure reducing valve operation Pressure relief valve operation Pipeline rupture Filter flushing operations Negative Pressure and Transient Pressure Measurement An excellent report and discussion of traditional methods to record transient and negative pressures in presented in the November 2004 AWWA Journal by Richard Gullick and several co-authors. (Gullick et al, 2004) Mechanical pen-and-chart recorders have been in use for decades, and offer a good solution to many pressure-recording needs. They are relatively inexpensive, easy to use and continuously monitor all pressures. The disadvantages of the mechanical recorders are that they need to be 2

manually reviewed and the charts need to be changed every day or every few days, are not typically designed for negative pressures, and they are not capable of providing detailed information on the duration of a transient since the width of the line drawn by the pen may cover up to 60 seconds of time. Figure 2 Circular graph recorder, with no negative pressure capability Several portable high-speed electronic data loggers are available. These do record negative pressures, and if set to record frequently enough can record the details of a specific surge event over a period of seconds to minutes. So if you know when the transient will occur and can set the data-recording rate accordingly, and can upload the data from storage immediately after the event, these devices may fulfill the need. Data recording intervals of 0.05 seconds (20 Hz) are available. Figure 3 Digital data logger for pressure measurement On the other hand, if there is a need to monitor over longer periods of time, the data interval will have to be set at a longer interval to stay within the memory capacity of the device. An interval of once per minute might be selected, which would provide 1440 3

pressure readings per day. Surely this would convince a distribution main owner that the pressure is rigorously and carefully monitored. But is this sufficient? Not necessarily, because many of the most damaging transients may last only a fraction of a second, and would not be detected at all. It has been difficult to detect and measure an unexpected transient that may last a fraction of a second, and that may be 100 times the operating pressure or more. Not only are these events difficult to detect, they may be the most damaging of all and may go unnoticed for long periods of time. Digital systems engineers will recognize this as the Nyquist principle. Figure 4 Digital data collection with insufficient sample rate A New Method of Pressure Measurement Within the last year, a system has been devised that overcomes several of the limitations of previous systems. It is capable of monitoring over extended period of time in a snoozing mode, recording background pressure at a user-set interval between once per second and once per day. Although the system appears to be snoozing, in reality it is very busy. It continuously samples the pressure 1000 times per second and computes a running average. Effectively the system algorithm has a built-in alarm clock that goes off when a pressure is detected that differs significantly from the average in other words when a transient is detected. When this occurs, the system wakes up and records all data at another user-set rate up to 100 Hz. This continues until the transient has passed, at which time the system goes back to the snoozing mode. The scheme is shown graphically in the figure below. 4

Figure 5 The TP1 Transient Pressure Monitoring System algorithm The so-called TP-1 Transient Pressure Monitoring System is comprised of A pressure transducer with an effective range fitted to the pipe being tested. For example, the range selected might be minus 14.7 to plus 500 psi for typical water transmission mains. A system controller, which processes all of the input signals, and performs all of the logic in the system. It also stores all of the historical data until it is retrieved using the PDA. A means of communication, such as a wireless-capable PDA or laptop. SCADA integration and internet have also been used. Data analysis software to facilitate data interpretation. Figure 6 TP1 Transient Pressure Monitoring System components 5

The TP-1 has been under development for nearly 2 years, undergoing extensive bench testing and modification. One of the early examples of data recorded with the TP- 1 include the acceptance testing of a new Wastewater Treatment by the City of Glendale, AZ. They had experienced the rupture of several 8 (20.3 cm) ductile iron pipes in the course of testing, and had attempted to diagnose the problem with a chart recorder. The test data from the chart was not very revealing. Figure 7 Circular graph of sewage lift station discharge pressure They installed a demonstration model of the TP-1 to see if it could detect the transients at the discharge line of the lift pump station. Figure 8 TP1 installed at sewage lift station 6

The results were such that when the City Engineer visited during the TP1 demonstration, his remark to the author was that this TP-1 is installed on a City facility, and had at that moment been appropriated by the City; he would not allow it to be removed. Figure 9 TP1 graphic depiction of the lift station pump shutdown sequence pressure (Note negative pressures to -14.5 psi) The data collected at the sewage lift station showed negative pressures approaching the cavitation range during the pump shutdown sequence. Remediation measures were installed to prevent damaging waterhammer events. The system allowed the careful evaluation of surge reduction measures, and continued to monitor the dynamic pressures at this $30 million facility during its early months of operational testing. A Hydrodynamic Pressure Test for New Distribution mains The availability of this new technology should open the door to new testing and improved asset management. For instance, some specifications for a new distribution main typically include a hydrostatic test to be performed by the general contractor to prove system integrity prior to final acceptance by the owner. This test may be slightly above the working pressure to demonstrate the structural capacity of the distribution main to withstand internal loads, while the makeup water volume is measured to demonstrate water-tightness. (AWWA Manual M9) It is typically accomplished under controlled conditions, with the pass/fail criteria being makeup water rate and absence of any indication of structural failure. This test is all well and good, but it misses the problem caused by transients in normal operation. 7

The author suggests that the time has come for us to include a Hydrodynamic Pressure Test in the specification for new transmission pain construction. This proposed test would not be in lieu of the traditional hydrostatic test, but in addition to it. To capture the capability of new technology to protect the interests of all parties, it is suggested that a paragraph in the specification for a new transmission main might read: Hydrodynamic Pressure Test - The CONTRACTOR shall engage the services of a THIRD-PARTY ENGINEERING FIRM to conduct pressure monitoring of the distribution main at the points designated below. The pressure monitoring shall be continuous during the initial filling of the distribution main, and throughout the acceptance test, and for period of 30 days following substantial completion of the project. All pressures, both positive and negative, shall be recorded not less frequently than once every minute throughout this period, except that any transient pressures shall be recorded not less than 50 times per second. A transient shall be defined as any sudden departure of more than 10 psi from the running 5-second average pressure. The THIRD-PARTY ENGINEERING FIRM shall submit interim reports following initial filling, and following the simulated power failure of the XYZ pumping plant; and a final report of all recorded pressures in graphic and tabular form. The graphic presentation shall depict a separate graph for each recorded transient in sufficient detail to observe each data point. The report shall compare the recorded pressures to the design pressures specified by the ENGINEER. The final report shall include calibration curves for the pressure transducers used in the test before the initiation of testing and upon completion of testing, and a certification that the equipment used is capable of meeting the requirements of this paragraph, and shall be sealed by a registered engineer. One copy of the final report shall be submitted to each the CONTRACTOR, the OWNER, and the ENGINEER. Points to be tested are: (to be determined by the design engineer, and should include locations vulnerable to transient and negative pressures e.g. pumping plant discharge lines, air valves, butterfly valves, pressure reducing valves, and pressure relief valves) The photo at the beginning of this paper might illustrate the point. As the Superaqueduct project in Puerto Rico neared completion, it was a textbook success story a tribute to the advantages of the design-build delivery system. It was an elegant water development project meeting an urgent need for the people of San Juan - ahead of schedule and under budget until the water main rupture of 9/11/99. This pipeline rupture was caused primarily by a butterfly valve that closed too quickly. The project had been properly designed and the proper control valves and valve actuators had been specified. The concrete pressure pipe had been properly manufactured. The general contractor had done an excellent job, except for one small detail. When the electricians wired the valve actuator, they eliminated a $5 closure-delay device, which caused the valve to close in 5 minutes instead of the 30 minutes specified by the designer. During operational testing, that valve was closed about fifteen times causing excessive and damaging pressures to the water main. The final closure on 9/11 was the straw that broke the transmission main s back, causing it to rupture in two locations. In the litigation that followed the rupture, damage estimates approaching $30 million were 8

described. If the Hydrodynamic Pressure Test had been required, that problem associated with the improperly wired valve actuator would have been recognized the first time it was closed. Clearly all parties to the construction would have benefited: the engineer, contractor, valve manufacturer, and facility owner. This new transient monitoring technology can be used to advantage at other junctures in the life of a water main, for instance: Upon substantial modification to the facility, such as the addition of a booster station Upon completion of any maintenance activities involving valves or pumps Upon addition of any delivery point or customer During periods of freezing weather, when air valves and siphon-prevention valves may become frozen and dysfunctional Periodically, as a matter of active distribution main management In Conclusion Advances in digital technology and equipment have opened the door to improved monitoring of negative and transient pressures. Owners, engineers, contractors, and operators are able to continuously monitor, detect and record these events that may be causing structural damage to distribution mains or contamination of water supplies. The greatest benefit of this capability may be through the implementation of a hydrodynamic pressure test, in addition to the standard hydrostatic pressure test, as part of the acceptance testing for new distribution main facilities. References Gullick, Richard W.; Mark W. Lechevallier; Richard C. Svindland; and Melinda J. Friedman; Occurrence of Transient Low and Negative Pressures in Distribution Systems, AWWA Journal 96:11, p. 52; November 2004 Worthington, Will, Monitoring for Transient Pressures in Pipelines; Proceedings, American Society of Civil Engineers Pipeline Conference; Houston, TX; August 2005; wworthington@earthlink.net, phone 480 748 3578 American Water Works Association, Manual of Water Supply Practices M9, Concrete Pressure Pipe, 1995. Advantica, Hydraulic Transients and Surge Control in Liquid Pipelines, 5177 Richmond Ave, Houston, TX 77056; 2005 9