## Best Practice No. 53 – Steam and Condensate System Leakage Costs

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**Steam and Condensate System Leakage Costs**

** **Steam and condensate leaks are unacceptable—and even abnormal—in today’s industrial steam and condensate systems. These leaks cost industrial plants millions of dollars in lost energy while increasing emissions, creating safety hazards, and lowering the reliability of plant operations. Therefore, one of the highest returns on a plant’s investment is correcting steam and condensate leakage and instituting operational changes to prevent any leakage from occurring again in the system.

The steam leak has the following effects:

- Energy loss: $26,935.00 per year
- Emissions: 597,979 CO
_{2}per year and 470 NO_{X}lbs. per year - Safety issue
- Reliability: a plant shutdown will have to occur to correct the leak
- Cost of steam: $6.25 per 1,000 lbs., operating 350 days a year, with a 75 psig steam pressure

Steam and condensate leakage is one of the top five opportunities for reducing energy and increasing reliability and safety in plant operations. Steam leaks result in the loss of both latent and sensible energy, while condensate leakage can be the loss of flash steam (latent and sensible energy) or just condensate, which is the loss of sensible energy. These losses add up—often to *as much as 9% of overall energy consumption*.

In fact, due to the high cost of these energy losses, the correction of steam and condensate leakage offers very lucrative paybacks. The greatest beneﬁt of a proactive steam and condensate leakage correction program is that most leaks can be corrected without expending capital.

** **

**EXAMPLES OF ENERGY LOSSES**

The following are examples of the energy losses from different steam leaks. Typically, threaded connections, which have the highest failure rate, will have the highest volume of steam passing to the atmosphere. Steam passing through the leakage point of threaded connections will increase in volume due to the wiredrawing effect.

Standard valve packing is second in volume of steam loss to the atmosphere, because of the older technology in valve packing and because the packing area can be sizable.

Figure 2. Steam Leak $12,434.00 per Year |

The steam leak shown in Figure 2 has the following effects:

Steam cost per 1,000 lbs. | $6.25 |

Steam pressure | 50 |

Steam loss (pph) | 237 |

Cost/hour | $1.48 |

Days/year | 350 |

Cost/year | $12,434.05 |

CO | 274,667 |

NO | 216 |

Safety issue | Yes |

Shutdown required for correction | Yes |

Figure 3. Steam Valve Leak $3,585.00 |

The steam leak shown in Figure 3 has the following effects:

Steam cost per 1,000 lbs. | $5.20 |

Steam pressure | 75 |

Steam loss (pph) | 82 |

Cost/hour | $0.43 |

Days/year | 350 |

Cost/year | $3,585.00 |

CO | 96,677 |

NO | 75 |

Safety issue | Yes |

Shutdown required for correction | Yes |

The steam leak shown in Figure 4 has the following effects:

Steam cost per 1,000 lbs. | $5.50 |

Steam pressure | 45 |

Steam loss (pph) | 491 |

Cost/hour | $2.70 |

Days/year | 350 |

Cost/year | $22,716.00 |

CO | 569,504 |

NO | 448 |

Safety issue | Yes |

Shutdown required for correction | Yes |

Figure 4. Steam Leakage $22,716.00 |

The total results from the three leakage points in the steam system are as follows:

Steam loss (pph) | 810 |

Cost/hour | $4.61 |

Cost/year | $38,735.05 |

CO | 940,848 |

NO | 739 |

That’s $38,735.00 per year for just three steam leaks. By making the necessary changes to the system, including updating to today’s technology, steam and condensate leakage can be eliminated.

**How to Determine Losses from Steam Leaks**

Napier’s equation is a well-accepted method for determining the leakage rate. However, most forms of the equation that are used in industry are very aggressive—many times too aggressive. The standard formula is based on the orifice being “converging” and “well-rounded.” This is rarely the case unless it is a steam trap orifice or a full-bore ball valve—as examples—that are discharging to the atmosphere.

Through its research and testing, Inveno Engineering has found that by adding a constant to the Napier oriﬁce equation, it can estimate a conservative steam ﬂow and energy loss from steam leaks.

**Estimating Steam Loss: Napier’s Equation**

**Steam Loss = 22.88 x Pa x D ^{2}**

Where: 22.88 is a constant

Pa (Pressure differential absolute)

D^{2} (Diameter squared)

Figure 5. Steam Flow |

Steam ﬂow through a leak can be calculated using a the above oriﬁce equation, which is based on the diameter of the leak, the pressure at the inlet of the oriﬁce, and the pressure at the outlet (atmosphere).

However, Inveno Engineering steam team members historically have identiﬁed the following leak characteristics in steam and condensate systems:

- The leak path is
*not*a perfect oriﬁce. - Determining the diameter of the passage is difﬁcult because the leak is not a perfect circle.
- Pressure at P
_{1}may not be measured or indicated and may have to be calculated based on methods.

Figure 6. Pressure Upstream and Downstream of a Leak |

Our upstream pressure and P_{2 }(outlet pressure) will be 0 psig because the steam and condensate leaks are discharging to the atmosphere.

There are many variables in determining the cost for steam and condensate leakage, such as the following:

- the true diameter of the leakage passage,
- the correct steam or condensate pressure at P
_{1}, - the restrictions that could affect P
_{1}pressure: for example, a steam leak on the outlet of the valve (calculate the pressure drop in the valve to determine P_{1}), and - leakage around valve packing or threaded connections.

If a pressure measurement or indication is not available for P_{1} and the steam is saturated, then the task of determining P_{1} is accomplished easily by using an infrared temperature measurement device. Saturated steam at a given temperature directly correlates to saturated steam pressure.

All factors must be considered when estimating the true cost of the steam and condensate loss.

Steam ﬂow through a leak can be calculated using an oriﬁce equation, which is based on the diameter of the leak, the pressure at the inlet of the oriﬁce, and the pressure at the outlet (atmosphere).

**How to Determine the Diameter of the Leak Path**

Figure 7. Estimating Leak Volume by Plume Length |

Even for the most experienced plant personnel, determining the diameter of the leak path is difﬁcult at best. Steam is extremely hot, and trying to measure the diameter of the path can be dangerous. Many times, the actual leak cannot be observed due to insulation or other factors.

Leaks can occur in the packing around a control valve stem, a union connection, a flange connection, etc. It is definitely not always easy to determine the actual size of the orifice (hole). Inveno Engineering recommends that plant personnel be trained with different tools to help visually determine the steam leak diameter from a safe distance.

** Note:** Using high-frequency ultrasound has been extremely helpful in determining the leakage volume, but the personnel using the equipment need to be trained on how to accomplish this goal.

Determining the steam leak volume by plume length is extremely difﬁcult and is not very accurate.

# 3. ROAD MAP FOR STEAM LEAKAGE

Changes need to occur imminently to achieve a leak-free steam and condensate system. The goal of a leak-free system is achievable with th