Energy Conservation Tips

Steam, a versatile and efficient energy carrier, is widely used across various industries. To optimise energy consumption and reduce operational costs, it’s essential to implement effective energy conservation measures in steam systems.

This guide will explore practical tips and strategies to enhance the efficiency of your steam systems.

energy-conservation-tips
  • Condensate is almost 20% of the fuel energy

  • Flash Steam Holds 50% of the Energy Content of the Condensate

  • Open vessels containing heated fluids should be covered

  • Advantages of Returning Condensate to Feedwater Tank

  • Return condensate as soon as it is formed.

  • Ensure Maximum condensate is returned to the feedwater system.

  • Condensate should be recovered.

  • Mixing high pressure and low pressure condensate increases the back pressure

  • Returning condensate by trap pressure often results in reduced condensate evacuation

  • Flash steam should be separated from condensate while returning the condensate to feedwater tank.

  • Recover Flash Steam From Contaminated Condensate

  • Use Steam at Lowest Possible Pressure for Indirect Heating

  • Use Steam Traps to Drain Condensate

  • Steam line tappings for equipment must always be taken from the top of steam pipes

  • Eliminate air steam system to ensure effective heating and thus fuel savings.

  • Advantages of Steam Operated Pumps

  • Tappings for steam traps should be taken through correctly sized drain pockets.

  • Keeping the insulation dry reduces radiation loss and thus saves fuel

  • Small leaks cost big money

  • Wet steam reduces the process efficiency

  • Avoid Group Trapping

  • Avoid Sagging of Steam Lines

  • Individual trapping lowers process time and reduces steam consumption.

  • Identify stall condition and take corrective actions.

  • Recover Blowdown Heat

  • For air heating equipment use heat exchangers with finned tubes

  • Stall increases steam consumption and process time

  • Use saturated steam for indirect heat transfer applications

  • Circulation pumps are not needed for hot water and thermic fluids

  • Stall increases steam consumption and process time of the heat exchanger

  • Using multi effect evaporators in place of single effect evaporators reduces the steam consumption by about 1/3rd.

  • Utility flows should be measured accurately

  • During product drying, lumps should be broken into smaller pieces

  • Strainers should be installed correctly so that they do not become a source of wetness

  • To reduce steam consumption, a pressure reducing station should be opted for

  • On Steam heating applications controlling the temperatures to set point avoids excess steam consumption

  • For hot water systems, usie indirect heat exchangers in place of direct injection based systems

  • Insulate oil tank in the tank farm

  • Use Indirect Heating for Hot Water Generation

  • Use Saturated Heat for Utilization in the Process

  • Use Diffusers at the Point of DIscharge for Steam Traps DIscharging to Atmosphere

  • Installation of a Vacuum breaker protects the process equipment

  • Use Vacuum Breakers on Small Heat Exchangers to Avoid Stalling

  • Moisture Separators Should be Insulated

  • Installing View Glass After a Steam Trap Eases the Maintenance

  • Installation of a Vacuum breaker protects the process equipment

  • Balanced Pressure Thermostatic Steam Traps Should be Used for Tracing Applications

  • The Temperature of Furnace Oil Day Tank Should be Regulated.

  • Balanced Pressure Thermostatic Steam Traps Should be Used for Tracing Applications

  • The Temperature of Furnace Oil Day Tank Should be Regulated.

  • Correct Installation of Air Vents

  • Correct Installation of Steam Traps

  • Install moisture separators to maintain dryness of steam.

  • Correctly sized steam mains are critical.

  • Importance of correct application based steam trap selection

  • Redundant steam lines should either be removed or blinded

  • Effective control while de superheating steam is critical to avoid steam losses.

  • Accumulated condensate in steam lines can lead to noisy and damaging water hammer

  • Steam Mains should be engineered to facilitate flow of condensate by gravity to the steam trap

  • Long saturated steam distribution lines should be sized on pressure drop method.

  • Use Steam Flow Meters With Ability to Compensate for Change in the Density

  • Pipe sizing should be done correctly to avoid losses during steam distribution

  • Increase in TDS levels in the feedwater tank leads to water carry over thereby increasing fuel consumption.

  • Monitor flue gas temperatures to control stack loss.

  • Co-generation plant operations should be decided only after comparing the running cost to cost of electricity.

  • Using steam instead of thermic fluids for indirect heating is more efficient.

  • Monitoring flue gas temperature gives a good indication of the boiler operating conditions

  • Boilers efficiency should be monitored.

  • At part loads the most efficient boiler should be used.

  • Poor quality of fuel leads to poor boiler efficiency.

  • Operating boiler closer to full load improves efficiency

  • The configuration of the co-generation system is important to ensure high efficiency

  • Chemical treatment of make up water increases the TDS levels in the boiler

  • Avoid Frequent Changes to the Boiler Fuel Firing System

  • Increase the inlet air temperature to increase boiler efficiency

  • Higher feedwater temperature increases the boiler output

  • Avoid High Negative Draft in Solid Fuel Fired Boilers

  • Use saturated steam for indirect heat transfer applications.

  • Generate Steam at Higher Pressure

  • Steam is preferable to thermic fluid as heating media.

  • The TDS inside a boiler should be maintained at recommended levels

  • Maintaining high TDS levels in the boiler drum results in water carryover

  • Dissolved oxygen should be removed from the feedwater tank

  • Avoid over sizing the boiler

  • Shell type steam boilers offer better fuel efficiencies as compared to coil type boilers.

  • Boiler operation parameters should be monitored continuously

  • Co-generation plant operations should be decided only after comparing the running cost to cost of electricity

  • Feedwater tank should be sized to be 1.5 times the peak steam demand.

  • Injection of flash steam and condensate into the feedwater tank should be via a deaerator head

  • Minimize Boiler Scaling

  • High feedwater temperature drives out dissolved oxygen

  • Opting for shell type boilers over coil type boilers leads to availability of good quality steam

  • Measuring specific fuel consumption gives a true reflection of your plant efficiencies

  • Air to fuel ratio should be monitored and controlled to minimize unburnts

  • Flue gas temperatures are a good indicator of excess air

  • Safeguarding Boilers against Fuel Explosion

  • Importanceof Steam Trap Selection and SIzing

  • Use shell type boiler to recover condensate.

  • Every 6oC rise in feedwater temperature reduces the fuel bill by 1%.

  • Referencing the boiler efficiency to the GCV of the fuel rather than the NCV gives a more accurate picture

  • Black or White Smoke is an Indicator of Improper Combustion

  • Efforts should be made to minimize addition of surface moisture content in fuel.

  • Maintaining the right level of water in the feedwater tank reduces the overall boiler feedwater TD

  • The Temperature of Furnace Oil Day Tank Should be Regulated

  • To deliver the same amount of energy, the flowrate of hot water will have to be 45 times than that of steam