Steam Trap Operation & Maintenance Joel Lemke, C.E.M. Emerson Process Management 18 May 2016 Emerson’s Five Business Platforms Process Management Industrial Automation Solving the process industry’s toughest challenges with predictable success any time, any place Revolutionizing manufacturing to operate faster, more efficiently and cost effectively Emerson Confidential Slide 2 Network Power Optimizing and deploying critical infrastructure for today’s mobile, always-on world Climate Technologies Innovating to help improve human comfort, safeguard food and protect the environment Commercial & Residential Solutions Making projects easier, safer and more efficient for professionals, contractors and homeowners Local History: “Rosemount Eng. Co.” Day One: Frank Werner, Vern Heath, and Robert Keppel establish Rosemount Engineering Co. with $8,000 1956 1961 Rosemount instruments in space with NASA Mercury capsule and Alan Shepard Rosemount 1151 Pressure Transmitter debuts 1969 Space shuttle Columbia maiden voyage with 300 Rosemount sensors on board Rosemount instruments on the moon 1976 1981 The World Leader in Pressure, Temperature, Flow and Level Instrumentation Emerson Electric Company acquires Rosemount Rosemount 1151 inducted into Smithsonian Institute Emerson Confidential Slide 3 1992 Topics Steam Basics & Terminology Steam Trap Function & Types Effects of Steam Trap Failure Trap Testing & Intervals Emerson Confidential Slide 4 Steam Loses Energy as it is Distributed Maximum heat transfer efficiency is when the steam is in the vapor state Steam loses heat to the surroundings as it flows (even though the pipe is insulated) Saturated steam reverts back to water as it loses energy – condensate STEAM Emerson Confidential Slide 5 Steam Traps steam pipe air CO2 As steam travels through piping, heat is lost to ambient Some steam condenses to water & collects in low points If not removed, this leads to: – – – steam Steam traps remove this condensate while minimizing steam loss Secondary purpose: vent air, CO2 & other “non-condensibles” condensate steam trap line Emerson Confidential Slide 6 Inefficient heat transfer Corrosion Safety & equipment damage concerns from water hammer Steam Trap To condensate return General Steam Trap Operation Outlet Orifice Steam and Condensate In Emerson Confidential Slide 7 Condensate Out Condensate Detection Common to all steam traps Self-acting valve that cycles open & closed Drains condensate while preventing steam loss Help vent air, CO2 and other gases Passive; no external power (uses steam pressure) Drains condensate through internal orifice – Orifice size selected for a particular “condensate load” (expected amount of water since last trap location) High failure rate: expected service life ~4-8 years if properly installed – can fail ‘open’ or ‘closed’ Emerson Confidential Slide 8 Steam Trap Sizing Like an orifice – relate flow to differential pressure – Flow rate = condensate load • Apply safety factor of 2-3 to estimated load and size for that load – ∆P = steam pressure – condensate return pressure Emerson Confidential Slide 9 𝑄𝑄𝑚𝑚~ ∆𝑃𝑃 Topics Steam Basics & Terminology Steam Trap Function & Types Effects of Steam Trap Failure Trap Testing & Intervals Emerson Confidential Slide 10 Steam Trap Applications 1. 2. 3. Process – at steam heating processes (heat exchangers, unit heaters, coils, vessels, etc.) Drip – every ~200 feet on steam distribution lines and before valves, pipe ends & changes in direction Tracer – small steam lines wrapped around process lines to maintain temperature, usu. so it can be pumped Emerson Confidential Slide 11 Steam Trap Operating Principles Velocity difference between condensate & steam Buoyancy difference between condensate & steam Temperature difference between condensate & steam Emerson Confidential Slide 14 Mechanical Thermostatic Thermodynamic Steam Trap Operating Principles Velocity: 1. Thermodynamic Disc Buoyancy: 1. Inverted Bucket 2. Float & Thermostatic Temperature: 1. Bi-metallic 2. Bellows Emerson Confidential Slide 15 Mechanical Thermostatic Thermodynamic Mechanical Float & Thermostatic Operation – – 2 separate mechanisms for condensate and air removal Float rises with increasing condensate level, opening discharge valve • – Thermostatic element on top vents air & noncondensables Inlet - above Applications – – Continuous discharge (usually does not cycle) Heavy and/or variable condensate load Process applications Strengths & Weaknesses – – – Great for variable condensate loads Excellent air venting Water hammer can crush float, causing failedclosed condition Emerson Confidential Slide 16 Rectangular, bolted cover in a vertical plane Round, eggshaped Outlet - below Mechanical Inverted Bucket Steam Traps Operation – – – Applications – – Condensate enters, flows under the bucket, and fills the trap body, completely submerging the bucket Condensate discharges through open valve Steam enters bucket, making it buoyant and closing the valve Heavy but steady condensate load Drip or Process with not much air Round, bolted cover Strengths & Weaknesses – Inlet Resistant to dirt, which settles at the bottom – “Loss of prime” – fails open – Mediocre removal of non-condensables Emerson Confidential Slide 17 Tall, cylindrical shape Thermostatic Bimetallic Steam Traps Operation – – – Applications – – Element composed of bonded dissimilar metals Steam increases element temperature, causing trap to close Sub-cooled condensate causes element to contract, opening the valve High-pressure applications to 6020 psi High air venting requirements Square bolted cover Strengths & Weaknesses – Fully-open on start-up – good venting of condensate & non-condensables – Can install horizontally or vertically – Corrosion can interfere with opening & closing – Hysteresis – fails open Very slow cycling (condensate back-up) Emerson–Confidential Slide 18 Outlet Inlet May have integral strainer Thermostatic Bellows Operation – – – Applications – – Element composed of liquid-filled bellows; liquid boils near steam temperature Steam causes liquid to boil, bellows to expand, and trap to close Sub-cooled condensate causes element to contract, opening the valve Light condensate loads High air venting requirements Strengths & Weaknesses – Fully-open on start-up – good venting of condensate & non-condensibles – Can install horizontally or vertically – Small and lightweight – Susceptible to water hammer Emerson Confidential Slide 19 – Slow-cycling (condensate back-up) Thermodynamic Thermodynamic Disc Steam Traps Operation – – – – Applications – Condensate enters & pushes the disc up, allowing venting through the trap Steam enters at high velocity (lower pressure), causing static pressure above the disk to force it onto its seat, closing the trap Static pressure over a larger area overcomes the inlet pressure As steam condenses, pressure above the disk drops & the trap cycles. High temperature/pressure Large hex-nut cover Strengths & Weaknesses Smallest overall – Small & lightweight size, fits in palm – Tight shut-off when new of your hand – Short operating life Emerson Confidential Rapid cycling on light loads – “machine gunning” Slide 20 – Inlet Outlet May have integral strainer Topics Steam Basics & Terminology Steam Trap Function & Types Effects of Steam Trap Failure Trap Testing & Intervals Emerson Confidential Slide 22 Steam Trap Function steam pipe Traps help remove air – air in steam lowers its temperature • air CO2 – Quality, scrap, rework issues steam 80# steam w/ 5% air ~ 4 degrees F cooler Traps remove “non-condensibles” (like CO2) – CO2 reacts with water to form carbonic acid – accelerated corrosion – Reduced heat transfer condensate Emerson Confidential Slide 23 – Scale, dirt, plugging, leaks, early component failure Steam traps ensure a reliable steam system Results of Steam Trap Failing Closed Stream traps remove condensate from piping preventing: Steam Blast Jolts Midtown, Killing One – Erosion and corrosion of piping reducing the lifespan of plant equipment – Inefficient heat transfer across heat exchangers, distillers, reactors and crackers If this steam is not removed not only is there inefficient heat transfer, but: – Safety hazard: Water in steam causing erosion/corrosion of plant equipment – Safety hazard: Water flashing to steam and causing pressure surges Emerson Confidential Slide 24 “State investigators have focused on a steam trap about 10 feet from the blast site, which should have removed cooled water droplets from the pipe.” New York Post The mayor said the explosion appeared to have been caused by cold water that reached the pipe. “Cold water apparently causes these to explode,” he said. The New York Times Click to read more: New York Post The New York Times Other Condensate Issues in the Distribution System Erosion & Corrosion – CO2 and water create carbonic acid – Scale, plugging, premature component failure Efficiencies – Liquid forms insulating barrier between steam and pipe wall • 1/100” water = Iron ½” thick Poor temperature control – 80# steam w/ 5% air ~ 4 degrees F cooler Freezing damage to steam coils, heat exchangers & other equipment Emerson Confidential Slide 25 Water Hammer Erosion from water droplet impingement on blades Insulation 20% of traps cause 80% of trap issues Steam Loss upon Failure $60,000 $50,000 $40,000 $30,000 275 225 $20,000 175 $10,000 125 $0 1/32 1/16 75 3/32 1/8 5/32 3/16 Internal Orifice Size 7/32 1/4 25 9/32 The higher the steam pressure and bigger the steam trap line; the more energy is lost The average inspection period for steam traps is annual “Average-quality traps may have just a 4-year life expectancy (which implies a 25% failure rate), while higher-quality steam traps may have an 8-yr life expectancy (12.5% average failure rate).” – Emerson Confidential Slide 26 Risko, J., Understanding Steam Traps, Chemical Engineering Progress, Feb 2011 Steam loss rises exponentially with operating pressure and line size Trap failures are “cumulative” Blow-through failures raise condensate return pressure – reduces capacity of all traps that are part of system – more water hammer in condensate return Traps fail closed – other traps need to drain more condensate Emerson Confidential Slide 27 Topics Steam Basics & Terminology Steam Trap Function & Types Effects of Steam Trap Failure Trap Testing & Intervals Emerson Confidential Slide 28 Steam Trap Testing Methods 1. 2. Visual: Confirm proper installation & identify external leaks Thermal: IR gun for inlet & outlet temperatures – – 3. Confirms flow through trap and in proper direction Thermal-only: about half as effective as thermal + ultrasonic Ultrasonic: Listen for proper cycling and detect blowthrough and plugged failures – Sound frequencies > 20 kHz Emerson Confidential Slide 29 Ultrasonic Testing of Steam Traps Emerson Confidential Slide 30 Value Can Be Assigned To Each Trap Pressure Orifice Diameter 0.100 inch 0.200 inch 0.300 inch 30 psig 75 psig 150 psig 250 psig 450 psig $949 $3,797 $8,543 $1,905 $7,619 $17,142 $3,497 $13,989 $31,476 $5,621 $22,483 $50,586 $9,868 $39,470 $88,808 Larger, higher-pressure steam lines Protect important plant equipment Have a large impact on process control Emerson [File NameConfidential or Event] Slide 32 Confidential Emerson Significant steam loss may occur from large or highpressure traps. Adjust inspection interval accordingly. Automated Steam Trap Monitoring Wireless Acoustic & Temperature Transmitter Provides visibility to issues with critical steam traps Detects failures in minutes so issues don’t wait until next survey Complement to good steam trap inspections Emerson Confidential Slide 33 Automated Steam Trap Monitor Installation Easily installed Non-intrusive Mounted using stainless steel bands Can be placed in tight spots, harsh environments and hazardous areas Non-intrusive Clamp on to pipe; no cutting No process downtime Emerson Confidential Slide 34 Mounts with supplied stainless steel bands Interpretation of Acoustic & Temperature Measurements Steam trap state calculated using algorithms within a software program Based on acoustic noise level, temperature, pressure and trap type Trap states include: Good, Blowthru & Cold Works with all trap vendors & types 250 200 150 100 50 0 250 200 150 100 50 0 Good Trap Blowthru Trap Cold Trap 250 200 150 100 50 0 Emerson Confidential Slide 35 Know the state of each steam trap Easily sort to find failed traps Emerson Confidential Slide 36 Differentiate between trap and device failure We can help identify critical traps with fastest payback Emerson Confidential Slide 37 Service Contract Scope Steam Trap Health Monitoring monthly service contract includes all hardware necessary to monitor traps. Emerson installs and maintains WirelessHART network and monitors steam trap health. Gateway Antenna Cellular Antenna Enclosure Contents: WirelessHART Gateway Cellular Modem Power Supply Steam Traps and WirelessHART Monitoring Devices Emerson Confidential Slide 39 Monitoring Service Architecture Data is fed into a secure cloud environment for failure and performance analysis Hardware is installed and commissioned on site by Emerson certified technicians Emerson Confidential Slide 40 Deliverable: Trap Failure & Energy Reporting Emerson Confidential • 41 Emerson Confidential • Slide 41 Steam Trap Inspection Best Practices Classify traps according to process criticality Classify traps according to loss potential Set inspection interval based on leak rate – Inspect when steam loss = $2500? • Determine correct dollar threshold based on your priorities New monitoring technology facilitates real-time detection of issues with critical traps – Automates inspection in challenging locations Emerson Confidential Slide 42 US Pulp and Paper Company Reduces Energy Loss with Wireless Acoustic Monitoring Challenge: Unnecessary steam venting identified as culprit of energy loss Solution: Rosemount 708 Wireless Acoustic Transmitters Results: – Data from acoustic sensors showed frequency of unwanted steam venting – Power plant operators made adjustments to reduce temperature and avoid wasted steam energy Emerson Confidential Slide 44 Steam Trap Operation & Maintenance Joel Lemke, C.E.M. Emerson Process Management 18 May 2016
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