- 

Safety Management Through Analysis 

NFS Safety Notices
Issue No. 98-02
November 1998 

- 

 

 

OFFICE OF NUCLEAR AND FACILITY SAFETY

Office of Operating Experience Analysis and Feedback 

U.S. Department of Energy

Washington, DC 20585 

DOE/EH-0560 

Issue No. 98-02

November 1998


Water Hammer


Contents


 

Notice Summary

This Notice contains information regarding the causes and hazards of water hammer events as well as recommendations for avoiding these events based on lessons learned from investigations of water hammer events. Office of Environment, Safety, and Health (EH) engineers have determined that more than 40 water hammer occurrences were reported at Department of Energy (DOE) facilities through the Occurrence Reporting and Processing System (ORPS) between January 1990 and October 1998. These accidents caused three fatalities, several serious injuries, and costly damage to facilities and equipment.

 

Applicability

This Notice applies to all DOE facilities with pressurized water or steam systems. It should be processed as an external source of lessons learned information as described in DOE-STD-7501-95, Development of DOE Lessons Learned Programs.1 EH encourages DOE managers to examine their facility design, operations, maintenance, and training to determine whether the water hammer lessons learned presented in this Notice are applicable.

 

Process Description

Water hammer, also known as steam hammer, is a pressure or momentum transient in a closed system caused by a rapid change in fluid velocity.2 It is classified according to the cause of the velocity change.

The types of water hammer include the following.

  • Valve-induced water hammer
  • Void-induced water hammer
  • Flashing-induced water hammer
  • Steam-propelled water slug
  • Condensate-induced water hammer

Valve-induced water hammer occurs when a valve is closed suddenly. This causes pressure waves to propagate through the water in the upstream direction from the valve. Suddenly closing a valve can also result in a temporary void downstream of the valve. When the void collapses, it causes pressure waves to propagate through the water in the downstream direction from the valve. This is shown in Figure 1.

Figure 1. Valve-induced Water Hammer

Void-induced water hammer occurs when a line refills after a void has formed, usually as a result of a suction break. When a valve is opened, admitting water to the line, the newly admitted water fills the void until it impacts the remaining water. This impact causes a pressure wave that propagates in both directions. This process is shown in Figure 2.

Figure 2. Void-induced Water Hammer

Flashing-induced water hammer can occur when water moves through a pressure drop to a region where the pressure is less than the vapor pressure of the water. Some water will turn to steam, cooling the mixture until the steam pressure is equal to the ambient pressure. The expansion of the steam propels the water forward and can compress it into slugs, as shown in Figure 3. When a slug impacts standing water or encounters a piping change, it generates a pressure wave or momentum transient.

Figure 3. Flashing-induced Water Hammer

A steam-propelled water slug can occur when a steam valve is opened, causing a pressure difference across a water slug. This difference accelerates the slug, which causes transients when the slug changes speed or direction, such as the outward impulse to an elbow, as shown in Figure 4. Because this type of water hammer causes momentum impulses instead of pressure waves, it tends to damage piping supports.

Figure 4. Water Hammer from Steam- propelled Water Slug

Condensate-induced water hammer is caused by rapid condensation of steam by subcooled water. It can occur in several different ways.

The most common condensate-induced water hammer is caused by steam flowing over subcooled water.3 The steam flow causes ripples in the water surface. If one of these ripples touches the top of the pipe, it can momentarily seal off a pocket of steam, which then condenses and collapses, causing a pressure wave. This is shown in Figure 5.

Condensate-induced water hammer causes the most severe water-hammer accidents and was the cause of three fatalities at DOE facilities.

Figure 5. Condensate-induced Water Hammer in a Horizontal Pipe

Another type of condensate-induced water hammer occurs when the flow of steam into subcooled water stops suddenly, e.g., by closing a valve. This is referred to as a water cannon. The remaining steam in the line condenses, drawing the subcooled water back into the line. When this water impacts the closed valve, a pressure wave is generated. This process is shown in Figure 6.

Figure 6. Water Cannon

 

Event Summaries

Condensate-induced water hammer is the most frequently reported type of water hammer at DOE facilities and was the cause of all of the fatalities and injuries and most of the monetary damage attributed to water hammer. The distribution of water hammer occurrences reported in ORPS is shown in Figure 7.

Figure 7. Types of Water Hammer Occurrences Reported in ORPS

1986 Event at Brookhaven National Laboratory

On October 10, 1986, a condensate-induced water hammer at Brookhaven National Laboratory injured four steamfitters, two of them fatally.4 One of the steamfitters attempted to activate an 8-inch steam line located in a manhole. He noticed that there was no steam in either the steam line or the steam trap assembly and concluded that the steam trap had failed. Steam traps are devices designed to automatically remove condensate (liquid) from steam piping while the steam system is operating in a steady state. Without shutting off the steam supply, he and another steamfitter replaced the trap and left.

Later the first steamfitter, his supervisor, and two other steamfitters returned and found the line held a large amount of condensate. They cracked open a gate valve to drain the condensate into an 8-inch main. They cracked the valve open enough to allow water to pass, but this was too far open to control the sudden movement of steam into the main after all the condensate had been removed. A series of powerful water hammer surges caused the gaskets on two blind flanges in the manhole to fail, releasing hot condensate and steam into the manhole. A photograph of one failed gasket is shown in Figure 8. All four steamfitters suffered external burns and steam inhalation. Two of them died as a result.

(CLICK BELOW FOR LARGE IMAGE)

Figure 8. Failed Gasket on Blind Flange

A Type A Accident Investigation Board determined that the probable cause of the event was a lack of procedures and training, resulting in operational error. Operators had used an in-line gate valve to remove condensate from a steam line under pressure instead of drains installed for that purpose.

The board also cited several management problems. There had been no Operational Readiness Review prior to system activation. Laboratory personnel had not witnessed all the hydrostatic and pressure testing, nor had all test results been submitted, as required by the contract. Documentation for design changes was inadequate. The board also determined that Brookhaven management had not been significantly involved in the activities of the steam shop.

1993 Event at the Hanford Site

On June 7, 1993, a condensate-induced water hammer fatally injured a journeyman power operator at Hanford.5 The operator was in the process of opening a steam system valve that had been closed for 8 months. The line was 840 feet long and the valve was inside a steam pit at the low end of the line, 11 feet below the high end.

The operator cracked open the valve but did not hear any flow in the pipe. He then opened the valve further, so that it was about 50 percent open. Hearing water hammer sounds, he attempted to close the valve but was unable to. A blanked-off 6-inch valve ruptured from the water hammer, releasing steam and water. The operator climbed out of the pit but later died from the effects of inhaling steam.

A Type A Accident Investigation Board determined that the pipe was full of water when the operator opened the valve and allowed steam into the line. They also determined that the resulting water hammer caused a pressure transient, which caused the blanked-off 6-inch valve to rupture.

The board determined that the direct cause of the accident was the operator opening the steam valve too quickly. He apparently found the valve easy to manipulate, and probably opened the valve over 50 percent in 1 to 2 minutes. They also found deficiencies in operational procedures and training, system design, equipment, and management systems. These deficiencies included inadequate training on condensate-induced water hammer, failure to follow procedures, inability to manipulate valves remotely, inadequate configuration management, inadequate attention to and resources for the safety of non-nuclear facilities, and failure to comply with Occupational Safety and Health Administration regulations.

1991 Event at a Georgia Hospital

In June of 1991, a valve gasket blew out in a steam system at a Georgia hospital.6 Operators isolated that section of the line and replaced the gasket. The section was closed for two weeks, allowing condensate to accumulate in the line. After the repair was completed, an operator opened the steam valve at the upstream end of the section. He drove to the other end and started to open the downstream steam valve. He did not open the blow-off valve to remove condensate before he opened the steam valve. Water hammer ruptured the valve before it was 20 percent open, releasing steam and condensate and killing the operator.

Investigators determined that about 1,900 pounds of water had accumulated at the low point in the line adjacent to the repaired valve, where a steam trap had been disconnected. Because the line was cold, the incoming steam condensed quickly, lowering the system pressure and accelerating the steam flow into the section. This swept the accumulated water toward the downstream valve and may have produced a relatively small steam-propelled water slug impact before the operator arrived. About 600 pounds of steam condensed in the cold section of the pipe before equilibrium was reached.

When the downstream valve was opened, the steam on the downstream side rapidly condensed into water on the upstream side. This flow picked up a 75 cubic foot slug of water about 400 feet downstream of the valve. The slug sealed off a steam pocket and accelerated until it hit the valve, causing it to rupture.

Investigators concluded that the accident could have been prevented if the operator had allowed the pipe to warm up first and if he had used the blow-off valve to remove condensate before opening the downstream valve.

1994 Event at the Savannah River Site

On June 16, 1994, a building supervisor opened a manual steam supply valve from the header to heating coils for a tank at Savannah River H-Canyon.7 A control room operator then opened a remotely operated valve downstream of the manual valve, allowing steam to enter the heating coils. About 10 minutes later, the building supervisor heard a hammering sound and saw steam coming from the area. He investigated and found steam leaking from the steam header isolation valve. He notified the operator, who closed the remotely operated valve.

The building supervisor then instructed the crane supervisor to close the building main isolation valve. Operators opened blowdown valves to drain condensate and reduce steam pressure. About 950 gallons of condensate were drained, which stopped the water hammer. The event lasted between 10 and 15 minutes and caused approximately $250,000 in damage to the steam header.

During the subsequent system walk-down, operators discovered that sections of the 10-inch steam header were displaced about 29 inches at a bellows-type expansion joint. A photograph of the displaced expansion joint is shown in Figure 9. Angle-iron pipe supports had failed during the water hammer, allowing the movement. The steam header and expansion joints were permanently deformed. Additionally, the steam header isolation valve gaskets failed and two cooling-water lines were damaged, as were instrument cables and cable trays.

(CLICK BELOW FOR LARGE IMAGE)

Figure 9. Displaced Steam Header at Bellows Expansion Joint

A Type B Accident Investigation Board determined that the direct cause of the accident was the opening of steam supply valves, allowing steam to flow through a water-filled steam header, resulting in condensate-induced water hammer. The board also determined that the header had been full of water because personnel had rendered inoperable the only steam trap for the involved section of the header when they closed a steam trap valve without authorization sometime between May 28 and June 13, 1994. The board determined that the root cause was management failure that allowed the steam system to be operated without adequately trained operators and without technical, administrative, and procedural controls in place that would have assured safe operation. Contributing causes included a lack of understanding of the principles of conduct of operations, failure to recognize unacceptable operating and maintenance procedures, lack of understanding of the fundamentals of steam theory and steam system operations, ineffective training in steam system operations, failure to provide some required procedures and to enforce procedure use, failure to upgrade procedures following the water hammer fatality at Hanford, and lack of an effective lessons-learned program.

Water hammer events continue to occur. The most recently reported DOE water hammer event occurred on October 25, 1998, at the Hanford Site while restoring steam following a three-day steam outage. On July 20, 1998, at the Hanford Site, a water hammer event occurred because an operator failed to open steam line drains before introducing steam into the line, as required by operating procedures.

 

Significance of Events

Water hammer has resulted in deaths, injuries, and property damage and has delayed operations at numerous DOE facilities. While water hammer events are being reported at a rate of only approximately five per year, the consequences of some of the events have been severe.

The potential for more water hammer events may be increasing because of a decline in the number of experienced system operators, age-related degradation of steam trap operability, and physical weakening of all system components.

 

Event Causes

In liquid systems, water hammer is most often the result of an operator closing a valve too rapidly. In steam systems, water hammer is most often the result of an operator either introducing steam into a piping system that contains liquid water or introducing steam into a relatively cool piping system too rapidly. In a significant number of events, poor system design was a contributing cause. Improper sizing of steam traps and incorrect location of traps were frequently cited as design problems.

Piping system component failures during a water hammer event result when the component strength is not sufficient to withstand the pressure surge. Older systems may contain components incapable of containing pressure surges, particularly when temperatures and pressures have exceeded design tolerances, causing weakness or embrittlement. For example, the valve that failed during the 1993 event at the Hanford Site was constructed of gray cast iron. Cast steel is the preferred material for such components. Similarly, the use of piping system component materials such as "bondstrand" fiberglass, polyvinyl chloride (PVC), and Teflon® (gasket material) is not recommended for steam systems. A steam system’s ability to withstand the pressure surges associated with water hammer can also be compromised by the cumulative effects of poor chemistry control and inattention to routine maintenance.8

 

Corrective Actions

For water hammer occurrence reports in liquid systems, facility managers frequently specify revising procedures and training to emphasize the importance of closing valves slowly. Where it is not feasible to close the valve slowly, a design change, such as a different valve design or the addition of air chambers or surge tanks to absorb all or most of the pressure rise, should be considered.9

For water hammer occurrence reports in steam systems, facility managers frequently specify corrective actions such as modifying the design or revising procedures.

The ideal system design has safe operation of the system as its principle objective. Safety depends on ensuring that proper condensate drainage (manual and automatic) and bypass valves are provided for all steam main isolation valves10.

In steam systems, steam must not be allowed to mix with water, either by injecting water into steam systems or steam into water systems. Steam and water cannot be mixed in a piping system without risking condensation-induced water hammer. Condensate should be assumed to be present in all low points and dead legs until proven otherwise.

Operators are expected to have the expertise required to operate steam systems safely. Managers can influence operator actions by requiring training, job hazard analyses, pre-job briefings, standard operating procedures, and direct supervision. Managers should also consider requiring operator aids such as pocket-sized cards or posters in the vicinity of major isolation valves listing important safety recommendations. The following safety recommendations should be incorporated into training and retraining programs for steam system maintenance technicians, operators, and supervisors. These recommendations should be followed regardless of piping size.

  1. Do not introduce steam into piping without verifying that no liquid water is present.
  2. Warm cold steam piping slowly, keeping blow-down valves for traps open.
  3. Walk down steam systems and check for proper location, distribution, and sizing of steam traps and blow-down valves for start-up and operation.
  4. Inspect steam traps frequently for proper operation.
  5. Do not crack open valves to avoid a condensation-induced water hammer. This will not guarantee safe operation. A steam-propelled water slug can form at very low flow conditions.
  6. Verify that traps are operating properly before opening steam line valves. On start-up, open blow-down valves fully and leave them open until liquid stops flowing.
  7. When feasible, operate valves remotely using mechanical extension linkage, reach rods, or power-operated valves. Ensure that reach rods and extension linkages are properly maintained.
  8. Inspect piping systems for sagging and, if necessary, install steam traps at low points or repair the sag.
  9. Check and repair piping insulation to reduce condensate formation in the piping and to save energy.
  10. All isolation valves should have bypass systems. Remember that bypass operation will not prevent water hammer if condensate is present.
  11. Do not use operational methods to permanently overcome design deficiencies in steam/water systems. Correct the system design.

Additional information related to water hammer training has been developed at the Hanford Site and may be obtained by contacting Steve Veitenheimer, (509) 373-9725, or Rick Barrickman, (509) 946-5102.

 

References

1 DOE-STD-7501-95, Development of DOE Lessons Learned Programs.

2 NUREG-0927, Revision 1, Evaluation of Water Hammer Occurrence in Nuclear Power Plants, March 1984.

3 Condensate Induced Water Hammer Safety Pamphlet, ICF Kaiser.

4 Report of the Investigation of the Steam Line Accident with Fatal Injuries on October 10, 1986 at the Brookhaven National Laboratory Operated by Associated Universities, Inc., November 14, 1986.

5 DOE/EH-0335P, Type A Accident Investigation Board Report on the June 7, 1993 U-3 Steam Pit Valve Failure Resulting in a Fatality at the Department of Energy Hanford Site, August 1993.

6 Kirsner, Wayne, "What Caused the Steam System Accident That Killed Jack Smith?" Heating/Piping/Air Conditioning, July 1995, pp. 37-53.

7 H-Canyon Condensation-Induced Water Hammer Accident, June 16, 1994, Type B Investigation Board Report, July 21, 1994.

8 DOE/EH-0437, Averting Water Hammers and Other Steam/Condensate System Incidents, June 1995.

9 Marks’ Standard Handbook for Mechanical Engineers, Ninth Edition, Section 3-70, "Mechanics of Fluids."

10 DOE/EH-9404, Occupational Safety Observer, April 1994.

 

Safety Notices Issued

  • Technical Notice 94-01, "Guidelines For Valves in Tritium Service," September 1994. 
  • Safety Notice 91-1, "Criticality Safety Moderator Hazards," September 1991. 
  • Safety Notice 92-1, "Criticality Safety Hazards Associated With Large Vessels," February 1992. 
  • Safety Notice 92-2, "Radiation Streaming at Hot Cells," August 1992. 
  • Safety Notice 92-3, "Explosion Hazards of Uranium-Zirconium Alloys," August 1992. 
  • Safety Notice 92-4, "Facility Logs and Records," September 1992. 
  • Safety Notice 92-5, "Discharge of Fire Water Into a Critical Mass Lab," October 1992. 
  • Safety Notice 92-6, "Estimated Critical Positions (ECPs)," November 1992. 
  • Safety Notice 93-01, "Fire, Explosion, and High-Pressure Hazards Associated with Drums and Containers," February 1993. 
  • Safety Notice 93-02, "Control of Temporary Modifications," September 1993. 
  • Safety Notice 94-01, "Contamination of Emergency Diesel Generator Fuel Supplies," July 1994. 
  • Safety Notice 94-02, "High-Efficiency Particulate Air Filters," August 1994. 
  • Safety Notice 94-03, "Events Involving Undetected Spread of Contamination," September 1994. 
  • Safety Notice 94-04, "Uninterruptible Power Supplies," November 1994. 
  • Safety Notice 95-01, "Decision Analysis Techniques," August 1995. 
  • Safety Notice 95-02, "Independent Verification and Self- Checking," September 1995. 
  • Safety Notice 95-03, "Lessons Learned Programs," October 1995. 
  • Safety Notice 95-04, "Post-Maintenance Test Programs," December 1995. 
  • Safety Notice 95-05, "Department of Transportation Non- Conformances by Vendor Shippers," December 1995. 
  • Safety Notice 96-01, "Chemical Spills During Loading," April 1996. 
  • Safety Notice No. 96-02, "Risk-Based Analysis of Electrical Hazard," May 1996. 
  • Safety Notice No. 96-03, "Compressed Gas Cylinder Safety," June 1996. 
  • Safety Notice No. 96-04, "Lightning Safety," August 1996 
  • Safety Notice No. 96-05, "Lockout/Tagout Programs," December 1996 
  • Safety Notice No. 96-06, "Underground Utilities Detection and Excavation," December 1996. 
  • Safety Notice No. 97-01, " Mixing and Storing Incompatible Chemicals" , June 1997.  
  • Safety Notice No. 98-01 , " "Electrical Safety," October, 1998.  

 


This notice is one in a series of publications issued by the Office of Nuclear and Facility Safety to share nuclear safety information throughout the Department of Energy complex. For more information, contact I-Ling Chow, Office of Operating Experience Analysis and Feedback, Office of Nuclear and Facility Safety; U.S. Department of Energy, Washington, DC 20585, telephone (301) 903-5984. This Safety Notice should be processed as an external source of lessons-learned information as described in DOE-STD-7501-95, Change Notice #1, Development of DOE Lessons-Learned Programs.


Safety Notices are distributed to U.S. Department of Energy Program Offices, Field Offices, and contractors who have responsibility for the operation and maintenance of nuclear and related facilities, and to other organizations involved in nuclear safety. Written requests to be added to or deleted from the distribution of Safety Notices should be sent to Christine Crow, RPI, 20251 Century Blvd., Germantown, MD 20874 or faxed to, (301) 540-2499.

The HSS Information Center maintains a file of Safety Notices and supporting information. Copies can be obtained by contacting the Info Center, (301) 903-0449, or by writing to HSS Information Center, U.S. Department of Energy, EH-72/Suite 100, CXXI/3, Germantown, MD 20874. Copies of Safety Notice are also available on the Operating Experience Analysis and feedback Home Page at http://tis.eh.doe.gov/web/ oeaf/lessons_learned/ons/ons.html. 

 

 

-
| Home | Performance Measures | Lessons Learned |
| ES&H TIS |
-
http://tis-hq.eh.doe.gov/web/oeaf/lessons_learned/ons/sn9402.html

Last modified: Thursday March 06 2008