Showing posts with label Contamination. Show all posts
Showing posts with label Contamination. Show all posts

Thursday, 20 October 2016

Best Strategies for Managing Varnish

Article extract from ReliablePlant newsletter:
http://www.machinerylubrication.com/Read/29354/managing-varnish-strategies

Varnish is the product of a chemical reaction within oil which leads to a new chemistry being created that is different from both the oil and its additives. A prevalent varnish begins as an acid, which is typically caused by a reaction of the oil’s additives as they become consumed or the base oil’s chemistry as it is degrading. It may also result from a reaction of the oil with other chemistries, which may be present as contaminants within the oil or the system. As with other lubricant-related properties or associated machine conditions, condition-monitoring techniques can be used to assess the accumulation of varnish within oil and manage the detrimental effects that follow.

Condition Monitoring

Lubricant condition monitoring involves obtaining data that supports an evaluation of the acceptability of the machine performance and the viability of the oil. To date, deposits on lubricated equipment have been the focus with regards to the detrimental effects of varnish. Figure 1 shows examples of bearings with significant varnish accumulation.

In general, the alarm and action criteria used within industry are set at levels to avoid power loss or machinery damage but may not include the prevention of varnish deposits. This discounts the effect varnish has on the design and performance of the oil and may allow oil to remain in service when it has exceeded failure criteria.

A principal area of lubricant condition monitoring that can often be overlooked is the suitability for continued use of the oil. This type of monitoring determines if the oil is able to meet its design properties. When outside of these criteria, the oil can be considered to be in a failure mode. Unfortunately, this aspect of lubricant condition monitoring appears to have become lost in comparison to the significant machinery impacts seen when varnish is found in turbine systems.


Figure 1. These heavy varnish deposits
were found on bearing surfaces.
(Courtesy Fluitec International)

If oil condition was the focus of monitoring rather than machine condition, then varnish likely would not progress to the point of accumulation and the oil would be much more capable of meeting its design. This type of lubricant condition monitoring should be emphasized when performing varnish-related monitoring since oil with a high varnish load can be expected to have critical loss in key design characteristics such as water separability and inhibiting corrosion/rust, foam and air release. Loss of any of these properties can place the system at significant risk. Testing criteria that focus on these properties should be at the forefront of the varnish issue.

Varnish Basics

The typical varnish progression begins with a reaction at the molecular level. This generally includes an oxygen molecule. In oil, the oxidized molecule is controlled through additives, which inhibit it from accelerating the degradation of the remaining oil. As more varnish forms, it becomes distinct particles that can be measured in nanometer-sized particles. As the numbers of these particles increase, this degradation material within the oil can be described as a varnish cloud of nanometer-sized material. When the cloud density oversaturates the oil, some of the varnish material will settle out within the lubrication system (like rain falling from the sky) in the form of a deposit. In time, the deposit can harden into a solid material, which is commonly known as varnish.

Oil Saturation

Turbine oil is designed to hold and manage a finite volume of varnish material. When this capacity is exceeded, the oil is considered saturated. Deposits can then form and accumulate in the system. Saturation has a relationship with temperature in that oil at a higher temperature is able to retain a greater volume of the nanometer-sized varnish material than oil at a lower temperature.


Figure 2. Varnish can occur in any system.
(Courtesy Paul Sly, Chevron)
The desired system condition for new oil would be to install the oil into a clean system so the progression of oil degradation and subsequent varnish accumulation would be limited to natural degradation of the oil. This degradation progression should be limited to the influences of new varnish created within the system as opposed to existing system varnish, which is known to accelerate oil oxidation.

It is important to install oil into a clean system so the maintenance sensitivity will more appropriately respond to the oil’s initial varnish saturation level as an oil failure criterion. This sensitivity should be maintained at the lowest expected system oil temperature rather than at a higher temperature, since deposits will form and collect in a system at this lower temperature, and deposit formation should be considered a lubricant failure mode.

Base Oil Influence

Varnish accumulation is also influenced by the base oil category, as designated by the American Petroleum Institute (API). Group II base oils have a superior design and can be expected to provide improved performance over Group I base oils, assuming that the system in which the oil is installed is clean. Both Group I and II base oils have inherent solvency, which means that they have a finite capacity to accumulate and hold varnish products. However, there is an important difference in how each does this. Due to the manufacturing process resulting in a more highly saturated molecule, Group II oils have less varnish-retention capacity than Group I oils. As such, Group II oils allow varnish deposits within a system to occur with a lower overall volume of the material present.

System Cleanliness

When a new charge of turbine oil is installed, it is vital that the system be clean and free of varnish. A common problem is that many existing systems are not cleaned prior to the installation of new/replacement oil. As mentioned previously, turbine oil has a natural design property that allows it to hold and accumulate varnish. In addition, existing system sludge and varnish that have adhered to surfaces within a turbine oil system are not readily dislodged with a system flush. As a result, when new, clean oil encounters this existing varnish within a system, it begins to chemically react with the varnish and remove this material from the walls, causing the new oil to approach a point of saturation.


Figure 3. Varnish deposits were
found within this system.
Within a relatively short period of time, this “chemical cleaning” phenomenon can render the benefits of a new oil change moot in terms of oil performance and design. In other words, the removal of system varnish may reduce the new oil to a “failed oil” status not long after it is placed in service.

The same condition occurs after a varnish-saturated oil is cleaned of varnish residue, but the cleaning is stopped prior to the system itself becoming clean. The newly cleaned oil will again accumulate varnish materials from the system to once again approach saturation levels. Remember, varnish acts as a catalyst to speed oil and additive degradation. As such, operating with varnish within the oil allows new varnish to form more quickly and shortens the service life of the oil.

Complications/Variations

The consequences of accumulated varnish within a turbine system can include power de-rating and damage to the operating equipment. When observed problems begin to occur, the concentration of varnish within the oil or system can vary greatly. Factors such as system design, variations in the system operating temperature and fluctuations in the system operating conditions all affect varnish formation.

Systems that use turbine oil as control oil are highly susceptible to issues. The control systems include tight orifices located in lower temperature regions. These conditions allow hot, saturated oil to accumulate deposits at these important system locations.

The choice of oil also impacts the rate of varnish generation and accumulation, as some oils are more prone to varnish drop-out than others. Figure 4 shows two samples with similar laboratory settling times. While these oils have a highly similar visual appearance, they have dramatically differing levels of varnish load, which is related to the influence of oil additives, base oil and the chosen formulation.


Figure 4. Different oil formulations can have very different
varnish conditions but appear highly similar.
(Courtesy Dave Wooton, Wooton Consulting)

Oils from different manufacturers are known to have different additives and base oils. Depending on the in-service operations, their differences can influence the severity of a developing varnish issue. Because these oil design variations are considered proprietary information by the lubricant manufacturers, the consumer of the oil is unlikely to be able to determine which oil formulation is least likely to cause varnish problems.

When system contaminants mix with the oil in service and further degrade it, the design properties such as water separation, foaming and the oil oxidation rate may be greatly compromised. As system design and operating conditions also vary, their impact should be considered as it relates to the select formula as well. This parameter of additive chemistry adds to existing varnish challenges for both oil performance and service life.

Laboratory Testing

The lubricant condition-monitoring community has developed a laboratory test (ASTM D7843) to assess the degree of accumulated varnish load within in-service oil. This Membrane Patch Colorimetry (MPC) test measures the overall load of varnish type material in the oil sample and includes a three-day settling period to allow varnish material to agglomerate within the oil, which is cooling from its operating temperature.

The oil is then filtered through a 0.45-micron cellulose patch with the aid of a solvent. Varnish material collects and deposits on the patch. The patch is checked for color, which is influenced by the volume of material deposited. A dark brown color is visible when more varnish from the fluid is on the patch surface.


Figure 5. The MPC test measurement of the sample on the
left was 24, while the sample on the right measured 156.
(Courtesy Dave Wooton, Wooton Counsulting)

Figure 5 shows side-by-side examples of a split sample of turbine oil that was allowed to sit for a two-week settling time under controlled conditions. The sample on the left was stored in the dark, while the sample on the right was left in the sun. The contribution of the sun is the difference in these samples, which have different colors and very different varnish loads.

Alarm Limits and Criteria

The lubricant test community is currently using various versions of the color patch test to assess the volume of varnish within oil and the likelihood of damaging deposits occurring. Unfortunately, the test variations in use may scale the color differently and provide differing warning and alarm limits. These differences can lead to significant confusion in the marketplace.

In addition, current alarm limits and action criteria focus on the effect of varnish accumulation on lubricated machinery. This approach discounts the impact of varnish on the design and function of the oil as well as the potential effect of this material on other oil failure modes.

3days of settling is included in a Membrane Patch Colorimetry (MPC) test to allow varnish material to agglomerate within the oil, which is cooling from its operating temperature.

A more fundamental approach to setting alarm and action limits that includes the impact of varnish on the oil’s performance is needed. The criteria should consider when the oil has lost its design performance, and these performance failure modes should be the point of initial action.

A temperature limit of oil saturation could become an important criterion. This could be measured by the patch test but at lower limits than those presently used in order to avoid machinery issues. This approach could then retain the present criteria as a higher severity warning for varnish and separate criteria for its potential challenge to machine operation.

Mitigation

Since oil that is in operation at a fully saturated level can be expected to leave varnish deposits, mitigation strategies to manage this condition should be directed at keeping varnish levels at a concentration where deposits would not be expected to form. The following are viable preventive maintenance strategies that have been demonstrated to benefit the system oil condition or varnish saturation level:

Partial or Full Oil Changes

As new oil does not have any retained varnish products, it would not be expected to cause new deposits when added to the system. However, the benefit of this method is severely limited by the quantity of varnish deposits within the system. When new (or newly cleaned) oil is placed in service, its inherent design results in cleaning the existing system varnish, which then goes into the oil. After this has occurred, the oil can again become saturated, and new varnish deposits can commence once saturation levels have been reached.

A secondary problem can develop from this mitigation strategy if varnish is removed from a less harmful area and then re-deposited in more undesirable locations. Another drawback in making frequent oil additions including full oil replacement involves the expense, as large volumes of oil can be costly.

While this approach could be beneficial if implemented in a manner that keeps the oil in a less than saturated condition, managing this would require frequent laboratory tests to ensure the oil condition. It is also questionable whether oil consumers would be sufficiently sensitive to the rate of varnish accumulation or change in the new oil to properly implement this method. However, it would produce a net benefit if performed periodically, as the cleanliness of the system in terms of existing varnish deposits can be improved with time.

Filtration with Cellulose Media

The best time to filter varnish material retained within oil is when the oil is at an ambient temperature for a few days. This allows the varnish to agglomerate and be collected by the filter material. Filter replacement is a must if this strategy is employed, as varnish material removed from the oil at ambient temperature returns to solution if the filter is not replaced prior to returning the oil to the higher operating temperature. This is due to the greater solvency of the oil at the higher operating temperature.

The primary limitation of this approach is that the filtration is limited to the reservoir oil and cannot be expected to reduce the volume of varnish within the main turbine system. When the oil returns to service, its inherent design is as a solvent, thus the results are removal of system varnish. Once again, due to existing system deposits, a saturation of the operating oil can reoccur.

In addition, varnish can migrate from a less harmful area to an undesirable location. The overall cost of this strategy can also be expensive, as frequent filter replacements could be required to remove system varnish from the varnish-laden filters. However, this method does produce a net benefit when performed periodically, and the cleanliness of the system in terms of varnish deposits can be improved.

System Chemical Cleaning

This method is the quickest way to improve system cleanliness and allow the oil to function as it was designed. While a clean system will extend the useful service of the new replacement oil, it cannot be expected to prevent reoccurrence of varnish. Its cost to implement can also be high.

Ion Filtration

With ion filtration, oil is processed through resin beads, which chemically attract the varnish component and remove it from the oil. This cleaning can occur at operating temperature. Ion filtration takes advantage of the oil’s design to slowly clean and remove existing varnish from the system as the oil is in service. With time, this process produces both a clean system and clean oil.

Conclusion

Mitigation strategies of ambient temperature filtration followed by filter replacement or installation of new oils can be used to manage varnish in systems if carefully employed. Of course, these strategies will carry the cost of additional oil and filter purchases. Regular laboratory testing also would be needed to manage these strategies and to monitor their effectiveness.

The introduction of Group II base oils as a fundamental component of turbine oils has not caused the varnish issues that plants are currently encountering, although their solvency and capacity to hold varnish were contributing factors. The change to a Group II base oil component has reduced the capacity of the fluid to retain varnish materials. Additional contributors include the formulation of the oil, the system design, the operating conditions and how much existing varnish is within the system.

81%of lubrication professionals have experienced problems caused by oil degradation products such as varnish and oxidation, according to a recent poll at machinerylubrication.com

A primary culprit of varnish problems occurring within industry can be directly attributed to the system cleanliness in terms of residual varnish deposits. The key to long-term varnish mitigation is in establishing a system free of varnish and then continuing a process that maintains both the oil and system in this condition. Ion filtration has been demonstrated to create these conditions, although once the system is clean, frequent oil additions or filter replacements may also be useful.

While the current industry focus regarding varnish has been on turbines, the same base oils and formulations are used for compressor, circulating and large motor/gearcase applications. Likewise, the same degradation mechanisms of the oil and additives would be present with subsequent varnish accumulations expected to occur. Such varnish deposits may be found on bearing and gear surfaces as well. Although the consequences of this accumulation and stress on oil properties have not been discussed, sensitivity to varnish should also be applied to these applications.

Alarm and action limits should be established to ensure system and oil cleanliness. This approach is challenged by long-standing plant operating expectations and experiences where varnish sensitivity was not required. The existing belief that there is an acceptable quantity of varnish within either the oil or system and that it is of no consequence must be overcome. Low action and alarm criteria should be set to protect the design and performance of the oil. In other words, a no-tolerance approach to varnish is required.

Monday, 17 October 2016

Oil Leakage: How Much of Your Profit is Going Down the Drain?

Article extract from ReliablePlant newsletter:
http://www.machinerylubrication.com/Read/29347/oil-leakage-drain

When it comes to oil leakage, at what point would you say enough is enough - 10 gallons, 100 gallons or 1,000 gallons? I recently started a lubrication process design where the client hadn’t reached the breaking point and was at 56,000 gallons of oil being lost per year due to leakage. When I explained it in terms of dollars lost (literally going down the drain), everyone’s ears perked up. It was a staggering sum. They had become complacent. It started as a small amount and grew week after week until they now have to bring in totes daily to set next to the trouble actors so they can feed them like an addict needing more and more.

As with every article I write, I like to consult the massive amount of material that is kept on subjects in Noria’s library. Thumbing through the files designated “leakage” could have consumed days on end. I found folder after folder of material dating back well more than half a century. I decided to read one of the oldest I could find, and it read as if it were written yesterday. Why do these problems still persist today? There have been great advancements in fittings, hoses, seals, etc., yet just last week I found myself almost wading through the basement of a steel mill.

While touring various plants, I am always amazed at how complacent they can become to leaks. I’m not sure they even realize the effects these leaks are having on their equipment, the environment and the morale and safety of the employees.

Possible Causes of a Leak

The following list does not include all of the possible root causes of a failure, but it does encompass the majority of the top contributors.

Improper assembly
  • There are multiple fittings on the market today. Making sure the fittings match is critical to their function
  • Over-tightening can lead to structural damage of the fittings.
  • Under-tightening will result in improper sealing.
  • Hoses that are too long or in a hazardous environment have a higher likelihood of being damaged.

Poor maintenance practices

  • Improper or lack of cleanliness while reassembling components
  • Becoming complacent with inspections or routine cleaning functions
  • Not fixing the source of the leak because it is easier to just top-up the sump

Adverse operating conditions

  • Large temperature swings can cause fittings to loosen over time.
  • Process waste and debris can eventually contribute to leakage.
  • High levels of particulate ingression can promote leakage.
  • Natural weather elements and sunlight can degrade seals.

Contamination

  • Contamination causes premature degradation of surfaces and seals.
  • An external leak not only will allow lubricant to exit the system but may also allow contaminants to enter.

Vibration

  • Excessive vibration can cause fittings and hoses to become loose and experience premature wear.
  • Hose abrasion is one of the most common causes of hose failure.

Loss of production, poor machine performance, environmental hazards, safety risks and high consumption costs all result from leakage and should be very important to the operation of any plant, yet I usually choose to investigate only one of these factors, as it is the one that seems to garner the most attention - cost. Keep in mind that the money saved from a fixed oil leak goes directly to the bottom line.

Inevitably, when discussing cost, the client wants to do a simple calculation based on the number of drops per second or minute vs. the cost of the oil. I will let them run through the calculation and arrive at a value. After we ponder the loss for a second, I will then ask, “What about the labor?” Don’t forget the benefits, management, planning, paperwork, etc. That’s not all. Used oil disposal, new oil testing, safety costs, cleanup, purchasing ... I could go on and on.


So while the number calculated at the beginning was already a jaw-dropping number, it didn’t include any of these other forgotten associated costs. The next statement from their mouth is typically, “What do we do?”

I prefer to take a preventive approach. First, develop a strategic plan that is both proactive and preventive. One of the easiest ways is to perform regular inspections with associated action items that are dependent upon the results of the inspections.

The second step is to control the operational conditions as best as possible. This is fundamental to any reliability and lubrication program, but simply keeping the machines and fluid clean, cool and dry will help mitigate the leakage.

Next, implement a detection and control program. Some popular leakage-detection techniques include visual inspections, dye injections/black light, system pressure decay, pressure differential, ultrasonics and flow meters.

66%of lubrication professionals use visual inspections to detect oil leakage at their plant, according to a recent survey at machinerylubrication.com

Finally, you must exercise proper contamination control. This not only will help with leaks but also will offer huge improvements in machine reliability.

It is estimated that more than 100 million gallons of fluid leak from machines every year in North America. How much are you contributing to this number? At nearly every plant I’ve visited recently, I can calculate enough money lost to employ an entire team of technicians whose sole purpose is to identify and stop leaks. Down the drain are going hundreds of thousands of dollars that could have been added directly to the bottom line. So the next time you walk by that small puddle on the floor or that drip from a fitting, I want you to see dollar signs.

.

About the Author
Jeremy Wright
Jeremy Wright is a Senior Technical Consultant for Noria Corporation. Hire Jeremy to develop procedures for your lubrication program or to train your team on machinery lubrication best practices. ... 

Thursday, 22 September 2016

Microdieseling and Its Effects on Oil

Article extract from ReliablePlant newsletter:
http://www.machinerylubrication.com/Read/29220/microdieseling-oil-effects

Would you consider 2,000 degrees F to be hot? At this temperature, aluminum, copper, gold and iron have already melted; stainless and carbon steels are glowing red; and your Thanksgiving turkey would turn into a charred mess in less than a second. So what is so significant about 2,000 degrees? Did you know that many hydraulic systems can create temperatures in this range?

Have you ever walked by a hydraulic pump that was cavitating? Once you hear it, you will never forget the signature sound it makes. I describe it as a can of marbles being shaken. What is actually happening is that the pressure acting on the fluid is below the saturation pressure of the dissolved gas (normally air) in the fluid. If the gas bubbles pass through a higher pressure zone (like that found on the discharge side of the pump), they will violently collapse. This alone can cause serious reliability issues with the machine component in terms of vibration, noise, surface damage and potentially failure.

37%of lubrication professionals have seen the effects of microdieseling, based on a recent survey at machinerylubrication.com

The compression of these bubbles in that pressurized side of the pump is adiabatic (not much heat is exchanged between the fluid and the bubble during the nanoseconds of increasing pressure).

For example, consider a hydraulic system with a suction-side air leak that lets in bubbles at a little less than atmospheric pressure and 100 degrees F and then pressurizes the fluid to 1,800 pounds per square inch (psi). The temperature in this example, which is typical of a hydraulic system with an air leak, would be just more than 2,000 degrees F.


When an air-ignitable mixture is present inside the bubble, ignition is almost inevitable at these incredible temperatures. This is the process known as microdieseling. It will lead to the oxidative degradation of the oil, higher operating temperatures, pressure spikes and the cavitational erosion of the hydraulic pump and other components.

The sources of the bubble formation within the system include but are not limited to:

  • Pressure drop through an orifice
  • Pressure drop through pipes and hoses
  • Turbulence from valves opening and closing
  • Shock waves due to sudden closing of valves and cessation of pump operation
  • Pressure drop due to the sudden opening of a valve
  • External force on a piston rod
  • Suction resistance
  • Plunging of fluid at the return to the tank
  • Inadequate net positive suction head available (NPSHA) relative to the net positive suction head required (NPSHR) in centrifugal pumps
  • Suction-side recirculation to sub-best efficiency point (BEP) operation of centrifugal pumps
  • Nearly dry operation of a pump due to insufficient fluid volume

Problems that result from the formation or presence of these bubbles include:
  • Oil temperature rise
  • Deterioration of oil quality
  • Degradation of lubrication due to viscosity loss or sludge and varnish formation
  • Reduced thermal conductivity
  • Cavitation and erosion
  • Noise generation
  • Reduced bulk modulus due to fluid aeration, leading to a spongy fluid and sluggish system control
  • Decreased pump efficiency
  • Reduced dielectric properties

    4 States of Air-in-Oil Contamination

    Dissolved Air - Air is completely dissolved in the oil and cannot be seen (no clouding).
    Entrained Air - Unstable microscopic air bubbles in oil.
    Free Air - Trapped pockets of air in dead zones, high regions and standpipes.
    Foam - Highly aerated tank and sump fluid surfaces (more than 30 percent air).

In layman’s terms, microdieseling is a pressure-induced thermal degradation. An air bubble will transition from a low or negative pressure area to a high-pressure zone and through adiabatic compression get heated to very high temperatures. These temperatures are high enough to carbonize oil at the bubble interface, resulting in carbon byproducts (sludge and varnish) as well as increased oil degradation (oxidation). In the best-case scenario, you would be able to stop the root cause of the problem - the bubbles. If you can control the bubble population, you can control microdieseling.


About the Author
Jeremy Wright
Jeremy Wright is a Senior Technical Consultant for Noria Corporation. Hire Jeremy to develop procedures for your lubrication program or to train your team on machinery lubrication best practices. ... 

Tuesday, 30 August 2016

How Particle Ingression Impacts Equipment Reliability

Article extract from ReliablePlant newsletter:
http://www.machinerylubrication.com/Read/29120/particle-ingression-reliability

Ingression can be defined as a going in or entering, a right or permission to enter, or a means or place of entering. If you have attended one of Noria’s Fundamentals of Machinery Lubrication courses, I’m sure you understand the importance of reducing, minimizing and eliminating particle ingression. Because of the negative impact particle ingression has on equipment reliability, it is critical to recognize the effects, how particles enter equipment and what you can do to reduce or eliminate ingression.

Particle ingression leads to contact fatigue, spalling, pitting, brinelling and cratering. Surface fatigue often develops from denting due to hard or soft particles. This creates a stress riser (berm). Repeated high loading (stress reversals) on berms or particles causes surface fatigue and eventually the formation of pits. This leads to larger pits followed by spalls.

85%of lubrication professionals say particle ingression has caused problems for their plant’s equipment, according to a recent survey at machinerylubrication.com

Particles can enter equipment through various means, such as through a process or a mechanical service that is performed after a failure or inspection. Therefore, it is paramount to take all precautions to minimize or eliminate any contaminants (dust, water, etc.) from coming into the equipment.



 “Six to seven percent ($795 billion*) of the gross national product is required just to repair the damage caused by mechanical wear.” - MIT Professor Ernest Rabinowicz

Most workers must deal with real-world conditions and may need to repair equipment out in the field. In these situations, take time to prep the area prior to opening an inspection door or bearing housing. This would include at the very least cleaning away debris from the inspection door or knocking off dust from overhead beams or adjacent machines.

Often it is the little things that make a big difference. Maintaining a clean area as well as clean tools and performing proper flushing of the equipment to remove any debris left behind can increase machine reliability. You have to give your equipment the best opportunity to perform its intended function, and minimizing or eliminating in-service ingression is essential to achieve this objective.

Ingression can also occur due to process conditions. This usually is the result of damaged seals or breathers and in-service equipment temperature changes, which can produce moisture within the machinery.



Faulty seals can allow contaminant ingression, which may lead to surface degradation. Machinery inspections should be performed routinely. Repairs, modifications and purchasing improved seals may be necessary to improve equipment reliability.

Keep in mind that not all seals are created equal. A proper assessment of your equipment as it pertains to temperature and the type of lubricant that you are using is crucial. Many times the lubricant and the seal may be incompatible, which can result in oil leaks. Remember, if you observe oil leaking out, there is an opportunity for contaminants to get inside the equipment.

3 Types of Particle Ingression

There are three general types of solid particle ingression: built-in, ingested and generated.

Built-in contamination consists of manufacturing debris such as burrs, machining swarf, weld spatter, abrasives, drill turnings, filings and dust. It can also include service debris that occurs when machines are opened for routine repairs and preventive maintenance.

Ingested particle ingression means that particles are coming into the machine and the lubricant under normal operating conditions (from the outside to the inside). These could be process particles (pulp, pulverized coal, ore dust, cement, clays, process chemicals, etc.), atmospheric contaminants (the result of ambient or road conditions near the machine), or combustion debris from internal combustion engines (soot, fly ash, induction air and contaminated fuel).

Generated particle ingression is when the machine makes its own particles. This can occur on internal surfaces through corrosion, mechanical wear, cavitation, exfoliation, etc. The oil also has the ability to break down and form particles (sludge, oxide insolubles, carbonization, coke, etc.).


The selection of breathers and monitoring breather condition provide another method of reducing ingression. Whether you are using them to eliminate dirt or water ingression, breathers are imperative for machine health. They must be selected according to the machinery conditions and environment. Frequently, breathers are not monitored properly. Like oil filters, they have an intended purpose and function well; however, once they reach the end of their life cycle, it is important to replace them promptly.

Remember, education is key. Understanding how ingression affects oil and equipment life is critical. Look beyond the obvious. Whether it is a color change of a breather, oil leaking from a seal, or water ingression in the oil, recognizing the effects of ingression can help you act promptly to improve machine reliability.