Reducing Emissions from Compressor Rod Packing Lessons Learned from Natural Gas STAR Producers Technology Transfer Workshop Devon Energy Corporation and.

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Presentation transcript:

Reducing Emissions from Compressor Rod Packing Lessons Learned from Natural Gas STAR Producers Technology Transfer Workshop Devon Energy Corporation and EPA’s Natural Gas STAR Program April 20, 2005

Page 2 Reducing Emissions, Increasing Efficiency, Maximizing Profits Agenda  Methane Losses  Methane Recovery  Is Recovery Profitable?  Industry Experience  Discussion Questions

Page 3 Reducing Emissions, Increasing Efficiency, Maximizing Profits Methane Losses from Production  Production responsible for 42% of methane emissions Transmission & Storage 98 Bcf Productio n 150 Bcf Processing 36 Bcf Distribution 73 Bcf 25 Bcf 10 Bcf 18 Bcf 1 Bcf Oil Downstream 2 Bcf Inventory of U.S. Greenhouse Gas Emissions and Sinks Emissions Reductions

Page 4 Reducing Emissions, Increasing Efficiency, Maximizing Profits Methane Losses from Compressor Rod Packing  Reciprocating compressors account for 2% of production sector emissions u Gas lost from rod packing is estimated to be over 350 MMcf/yr costing over $1 million (gas price of $3/Mcf) Inventory of U.S. Greenhouse Gas Emissions and Sinks Pneumatic Devices 60 Bcf Meters and Pipeline Leaks 11 Bcf Gas Engine Exhaust 12 Bcf Well Venting and Flaring 12 Bcf Storage Tank Venting 23 Bcf Other Sources 15 Bcf ReciprocatingCompressors 3 Bcf Dehydrators and Pumps 14 Bcf

Page 5 Reducing Emissions, Increasing Efficiency, Maximizing Profits Compressor Rod Packing What is the Problem?  Rod packing accounts for 12% of reciprocating compressor emissions in production sector u Over 44,000 reciprocating compressors in natural gas industry u Over 31,000 compressors in gas production sector Compressor Station Compressor Station Production 31,750 Compressors Processing 4,250 Compressors Transmission & Storage 8,000 Compressors Distribution 0 Compressors Compressor Station

Page 6 Reducing Emissions, Increasing Efficiency, Maximizing Profits Methane Losses from Rod Packing  Reciprocating compressor rod packing leaks some gas by design u Newly installed packing may leak 11 cubic feet per hour (cf/h) u Worn packing has been reported to leak up to 900 cf/h

Page 7 Reducing Emissions, Increasing Efficiency, Maximizing Profits Reciprocating Compressor Rod Packing  A series of flexible rings fit around the shaft to prevent leakage  Rings held in place by springs and packing cups

Page 8 Reducing Emissions, Increasing Efficiency, Maximizing Profits Methane Loss Sources from Rod Packing  Leakage occurs u Around packing case through nose gasket u Between packing cups u Around rings due to movement of the piston rod u Between rings and piston rod  Leaking gases escape either through vents on the packing flange or into the distance piece  Leakage gradually increases from normal wear of rings and rod

Page 9 Reducing Emissions, Increasing Efficiency, Maximizing Profits  Leak rates from rod packing eventually increase to a level that economically justifies packing replacement u Frequency of economic replacement depends on lubrication, rod alignment, rod wear, rod material and economic hurdle-rate  Benefits of economic packing replacement u Reduced methane emissions u Gas savings with lower leakage rates u Extended service life of compressor rods Methane Recovery with Economic Rod Packing Replacement

Page 10 Reducing Emissions, Increasing Efficiency, Maximizing Profits Rod Packing Replacement Decision Process Compare current leak rate to initial leak rate to determine leak reduction expected Monitor and record baseline packing leakage and piston rod wear Assess costs of replacements Determine economic replacement threshold Replace packing and rods where cost-effective

Page 11 Reducing Emissions, Increasing Efficiency, Maximizing Profits Establish Baseline Leaks  Step 1: Monitor and record baseline leakage and rod wear u Measure leaks immediately after installing new seals (or new rods and seals) u Monitor rods periodically for shaft dimensions and surface roughness when replacing rings  “Out-of-round” rod seals poorly causing uneven wear and allowing more leakage  It also causes uneven wear on the seals shortening the life of both seal and rod

Page 12 Reducing Emissions, Increasing Efficiency, Maximizing Profits Establish Leak Reduction Expected  Step 2: Compare current leak rate to initial leak rate to determine leak reduction expected u Leak Reduction Expected (LRE) = Current Leak Rate (CL) – Initial Leak Rate at the last ring/ rod replacement (IL) u Example: The current leak rate is measured as 50 cf/h, the same component leaked 10 cf/h when first installed LRE = 50 cf/h – 10 cf/h LRE = 40 cf/h

Page 13 Reducing Emissions, Increasing Efficiency, Maximizing Profits  Step 3: Assess cost of replacements u Packing ring replacement costs depend on the number of cylinders and the type of ring  Cost of a set of rings:$ 500 to $ 800 (with cups and case)$1500 to $2500 u Rod replacement costs vary with rod dimension and rod type  Cost of Piston Rod:$1800 to$3500 u Installation costs roughly equal equipment costs Assess Costs for Economic Rod Packing Replacement

Page 14 Reducing Emissions, Increasing Efficiency, Maximizing Profits Replacement Threshold for Economic Rod Packing Replacement  Step 4: Determine economic replacement threshold u Economic replacement threshold defines the specific point at which it is cost effective to replace rings and rods u Discounted cash flow method  Economic replacement threshold (cfh) = (CR*DF*1,000) / (H*GP) where, CR = cost of replacement ($) where, CR = cost of replacement ($) H = hours of compressor operation per year H = hours of compressor operation per year GP = gas price ($/Mcf) GP = gas price ($/Mcf) DF = discount factor = i*(1+i) n / (1+i) n – 1 DF = discount factor = i*(1+i) n / (1+i) n – 1 i = discount rate or company hurdle rate i = discount rate or company hurdle rate n = payback period selected n = payback period selected

Page 15 Reducing Emissions, Increasing Efficiency, Maximizing Profits Is Recovery Profitable?  Step 5: Replace packing and rods when cost effective u Example: Rod and Rings Rings:$1,200 Rod:$7,000 Gas:$3/Mcf Operating:8,500 hrs/yr Rings Only Rings:$1,200 Rod:$0 Gas:$3/Mcf Operating:8,500 hrs/yr Based on 10% interest rate Mcf = thousand cubic feet, cfh = cubic feet per hour

Page 16 Reducing Emissions, Increasing Efficiency, Maximizing Profits Industry Experience on New Rod Packing Material and Coatings  New packing materials can improve the life and performance of equipment u Carbon impregnated Teflon® rings cost almost the same as bronze rings but last about one year longer  Other factors like proper installation, cooling and lubrication play an important role u Piston rods coated with tungsten carbide or chromium increase service life of rods u Axially loaded packing installed in one of the last two cups reduces emissions

Page 17 Reducing Emissions, Increasing Efficiency, Maximizing Profits Axially Loaded Three Ring Rod Packing

Page 18 Reducing Emissions, Increasing Efficiency, Maximizing Profits Discussion Questions  What is your practice on replaced rod packing in reciprocating compressors?  How can the Lessons Learned study be improved upon or altered for use in your operation(s)?  What are the barriers (technological, economic, lack of information, regulatory, etc.) that are preventing you from implementing this technology?