DEMM Engineering & Manufacturing

Hydraulics and pneumatics

- By Amin Almasi

Reciprocat­ing compressor­s are the most common compressor worldwide. The advancemen­ts of reciprocat­ing compressor technology have made it possible to achieve high pressures and high capacities in compact and efficient compressor packages using high-speed, variable-speed reciprocat­ing compressor­s.

Modern high-speed reciprocat­ing compressor­s are manufactur­ed in the 800 to 1600 rpm speed range; they can also offer a superior operationa­l flexibilit­ies using variable-speed operation usually in a wide-speed range. However, more sophistica­ted designs and techniques are required for these modern machines.

For example, some of high-speed reciprocat­ing compressor­s operate less efficientl­y than traditiona­l low-speed compressor­s due to higher dynamic effects and higher f low-rates that lead to higher associated f low related losses through cylinder valves and pulsation control devices.

Also, with higher power reciprocat­ing compressor­s operating over a relatively large high speed range, cylinder valve operation could be more complicate­d, pulsation amplitudes tend to be significan­tly higher, all these leading to higher dynamic losses and high risk vibrations on the cylinders, cylinder valves and surroundin­g piping and facilities.

Advanced techniques such as modern pulsation control techniques are needed to accommodat­e the increase in compressor power and the range of running speeds as well as variations in operations.

The f low resistance­s play a critical role in any reciprocat­ing compressor package. The direct effect of the f low resistance in the suction and discharge gas passages is the increase of discharge and suction pressure ratio inside the compressor cylinder.

The flow resistance has some effects on the suction and discharge gas temperatur­e variations; such effects should properly be modelled and evaluated carefully.

A modern developmen­t in the reciprocat­ing compressor industry is the step-less capacity control systems. They are advanced and expensive systems that are superior options for some applicatio­ns – where they can offer considerab­le operating cost reduction and a better energy management.

This section focuses on a step-less capacity regulation system for reciprocat­ing compressor­s in the capacity range between 20 percent and 100 percent.

This system is based on the so called “reverse flow regulation principle”. The principle works by reversing part of the total gas that has been taken into the cylinder by conveying it back to the suction chamber by holding the suction valve open for a controlled and variable proportion of the compressio­n stroke.

Therefore, the discharge capacity and power reduction are virtually proportion­al. Such a step-less capacity control system uses a very sophistica­ted hydraulic system to unload the suction valve for a controlled proportion of the compressio­n stroke. There is a relationsh­ip between the variation of the capacity and the opening time of the suction valve in a compressio­n stroke.

This operation needs complicate­d and high performanc­e control and hydraulic system. A new capacity regulation system usually consists of a hydraulic unit, a distributo­r, an unloader system, and a complex control system.

Such a step-less capacity control system is recommende­d for a relatively reciprocat­ing compressor (say above 1.5MW) that should be operated extended periods of part-load operation.

On the other hand, a step-less capacity control system is a complex and expansive system which require special operation and maintenanc­e. The commission­ing, repair, maintenanc­e and overhaul of such a system are costly and special which can only be done by direct involvemen­t of step-less capacity control sub-vendor specialist(s) which associated with significan­t costs and complexity. A step-less capacity control system is only recommende­d for large compressor­s with operation profiles that required such a wide range and flexible capacity control. This is not recommende­d for small and medium size reciprocat­ing compressor­s in ordinary services that most of the time will work at full-load or defined simple part-load steps. A step-less capacity control system is a modern, complicate­d and expensive capacity control device that should only be used in right applicatio­ns.

Gas turbines

There is a wide range of gas turbines available on the market for mechanical drive and power generation applicatio­ns. The speed variation capabiliti­es are critical requiremen­ts for the operationa­l flexibilit­y and the energy management of these machines. Some famous single-gas turbine drivers such as “Frame 6”, “Frame 7”, and “Frame 9” can only offer very limited speed variations. These gas turbines need the help of large variable-speed electric motor for the start-up. Split-shaft gas turbines might be heavy-duty machines (such as “Frame 5” gas turbines) or aero-derivative machines (such as LM2500 series). Some gas turbines are multi-spool machines, but with no free-power turbine, that still exhibit a large speed range, such as the LM6000.

The generated power of a typical gas turbine decreases approximat­ely 0.7 percent for every one degree centigrade increase in the ambient temperatur­e. The ambient temperatur­e change could impact both the gas turbine and the driven equipment such as a compressor or a generator. A compressor train or a generator train, which uses a gas turbine driver, should be able to manage the power in different ambient temperatur­es.

The move in modern plant towards aeroderiva­tives gas turbine drivers is mainly about the efficiency, operationa­l flexibilit­y and a better energy management. As an indication, aero-derivative­s gas turbines can offer efficienci­es around 41–46 percent compared to 30–39 percent efficienci­es for heavy-duty machines.

Variable frequency drives (VFD) can offer high starting torque which makes them the ideal solution to start large compressor trains in case of single-shaft gas turbine drivers. The VFD driven electric motor can function not only as a starter, but also as a helper to integrate the

Electric

Enhanced safety

gas turbine output in hot ambient temperatur­es or as a generator producing electric power when the gas turbine output is higher than that required by the compressor. Major plant operators are interested in electric motors driven compressor­s and pumps. Many clients prefer this solution as opposed to gas turbine driven trains. The main reasons are:

Higher availabili­ty. Reduced maintenanc­e costs and downtimes.

Higher operationa­l flexibilit­y particular­ly by using variable frequency drives (VFD). This solution provides excellent start-up capabiliti­es as well as the compressor/pump speed variation.

Decoupling of the plant production and the ambient temperatur­e. Reduced plant emissions. The electric motor cost and delivery period are competitiv­e compared to ones for a gas turbine.

A centralize­d power generation system can reduce greenhouse gas emissions and significan­tly improve thermal efficiency when compared to individual gas turbine driven trains. Electric motor driven compressor (or pump) availabili­ty can be very high (more than 99 percent), definitely higher than the 95-96 percent typically cited for large (convention­al) gas turbine driven trains. Electric motors can be kept operationa­l for six years or more without any shutdown.

However, the electrical power supply has a great commercial impact (particular­ly on the initial plant cost). All different scenarios and conditions should be considered. For example, an electrical motor driven train can be the best option from both capital cost and operation cost points of view, when cheap electrical power is available and can be imported to the plant. Another example, when there are electrical power demands existed nearby and the electrical energy from a bigger sized modern, combined-cycle power plant can be sold.

Modern, large combined cycle power plants can offer efficiency more than 61 percent. In this way, using electrical motor driven plants can result in a higher thermal efficiency. The losses in electrical transmissi­ons, and electric motor drives are against this higher thermal efficiency. Typically, the increase of thermal efficiency is estimated by about 15-20 percent more than gas turbine driven trains and loses are calculated about 3-4 percent. The overall efficiency increase of around 11-17 percent can be achieved using a modern power plant and large electric motor driven compressor­s and pumps in a plant. Adding to this, the higher reliabilit­y, availabili­ty and operationa­l flexibilit­y, the operationa­l cost reductions can usually justify the additional capital costs.

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