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Karl Mueller - Industrial Specialist
Aerzen USA
(770) 951-7035
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Performance - Only buy Aerzen's blower packages... just kidding, but there is a serious point here. Any manufacturer's claims of performance need to be verified to insure the correct amount of pressure will be generated for the application. Insist on knowing the performance and efficiencies (power requirements) of the complete blower package you buy not just the performance of the bare stage. An undersized drive motor will limit performance.
Package design - Buy a complete package from the manufacturer when possible. A package assembled by others can consist of mismatched components that could have a negative impact on the blower's performance, and ultimately, its warranty.
Pricing - I put this last, because it is the least important component in the blower selection process. A decision based solely on a lower up-front capital cost can end up costing much more in the long run when cost of ownership is evaluated and the inappropriate, and possibly, less reliable equipment was selected.
Steve Lungstrum
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The refinery flare gas can be considered one of the most challenging, but it can be handled with the right compressor.
So how can we compress flare gas from a refinery?
Several types of compressors are being used.
Centrifugal compressors should not be recommended in refinery flare gas applications because they cannot easily deal with wide swings of mole weight and are sensitive to any solids or liquids entrained by the gas stream.
Positive displacement machines are best suited for these conditions because they can handle easily wide changes in the composition of the gas. I know of five types of mechanical compressors being used, more of less successfully in flare gas applications:
Each of these technologies has its place and can be successful when applied correctly.
A few pros and cons of each of these types of machines:
Sliding vane compressors are simple compressors with a single shaft off-center in a cylindrical housing. They work best in low pressure clean gas applications. They are not very reliable when dust or liquid is ingested in the machine and prevent the vanes from sliding back-and-forth in the rotor slots. Jacket-cooling is required and oil needs to be injected continuously for lubricating the vanes that slide along the housing. They may require relatively frequent overhauls, but these are relatively easy to handle. Initial costs are low.
Like the sliding vane compressors, the liquid ring compressors are also simple machines. The principle of operation is very similar to that of sliding vane compressors with the exception that a ring of liquid, generally water, is used instead of vanes that slide radially. Liquid ring compressors are therefore well suited for wet gas,
1) Type of compressor: positive displacement or dynamic
2) Type of compression: oil free or oil injected
3) Construction of compressor: gastight, hazardous gas or atmosphere, compressor metallurgies, instrumentation, motor type and manufacturer
4) Operation of compressor: variable ambient conditions, variable flow and/or pressure requirements, variable properties of the air or gas
Type of compressor is the first and most important selection criteria. A dynamic compressor will typically provide for small fluctuations in flow and discharge pressure through the use of guide vanes and/or throttle valves. These compressors operate in-between choke and surge regions and the vanes/valves help the compressor to run at its most optimal point. With the use of VFD the flow/pressure curve can be shifted on the performance curve to provide some variability.
These compressors are well suited for applications in which the flow/pressure doesn't vary more than 30%, or the ambient conditions or air/gas composition doesn't exhibit swings of more than 30%. The positive displacement compressor will provide a relatively constant flow regardless of what the pressure requirement is. With the use of a VFD this machine can provide for many applications with varying flow and pressure requirements.
The positive displacement is typically simpler than a dynamic compressor since it does not require the use of guide vanes, throttle valves, or sophisticated instrumentation. Finally, the buyer will need to determine if the compressor will need to be 100% oil free or oil injected. The oil injected machines can include oil separation and filtration to lower the oil content in the gas down to a few ppm. Some applications can handle this while others cannot, especially if the downstream oil accumulation over time is detrimental to the process.
Oil-free compressors are most often used in process gas applications. Hazardous, poisonous or simply dangerous gases are usually being compressed and conveyed by our screw compressors. It is critical therefore, that such conveying media be sealed against leaks to the atmosphere or, in the case of gases incompatible with lubrication oils, against leaks into the compressor's lubrication system. Dry gas sealing systems are often applied for such tasks.
Dry Gas Seals
Dry gas seals are mechanical face seals. They consist of a stationary (primary) ring and a mating, rotating ring. During operation, grooves in the mating ring generate fluid-induced dynamic forces, causing the primary ring to separate from the mating ring, thus creating a gap between them. A typical value of the running gap between the primary and mating rings is 3 to 4 microns. A sealing gas in injected into the seal, providing the seal between the atmosphere (or the oil system of the compressor) and the compressor's conveying chamber. Typically, a labyrinth seal separates the gas seal from the process gas, while a barrier seal, also a labyrinth seal, separates the gas seal from the compressor's bearings and their oil lubrication system. Barrier seals are buffered with gas - typically nitrogen, at a fixed pressure, and vented to the same vent as the seal gas exiting the dry gas seals.
The pressure of the seal gas is controlled, such that it is slightly higher (typically 0.3 bar, 5 psi) than the process gas pressure. Thus, part of the seal gas volume will leak into the process gas, while part of the barrier gas volume will leak into the compressor's bearings and then into the lubrication system, eventually reaching the oil tank. A vent is provided, such that the excess seal
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