Compressor Monitoring | PROGNOST Systems

Continuous vibration monitoring

Why monitoring of reciprocating compressors ?

Bahia de Bizkaia as a project involves the construction and commercial operations of an LNG regasification plant (Bahia de Bizkaia
Gas), which will have an annual regasification capacity of 800 000 Nm3/h, and an 800 MW combined cycle power plant (Bahia de Bizkaia Electricidad). The starting point for Bahia de Bizkaia lies within the energy strategy devised by the Basque government, which has been brought about by means of several energy plans. The liberalisation of the electricity market paved the way for another project: the construction of a combined cycle power plant (Bahia de Bizkaia Electricidad). This was intended to make the most of the possibilities offered by the regasification plant, as well as benefit from the different synergies between both projects, and help correct the shortage of power production in an area which, as mentioned above, has a great demand for this kind of energy, but not enough generation capacity.


The total investment for the project amounts to € 655 million; € 338 million has been invested on the power plant (Bahia de Bizkaia Electricidad), and the remaining € 317 million has been invested on the regasification plant (Bahia de Bizkaia Gas, BBG). Table 1 reflects the current trend towards a continuous increase in gas consumption and production.

Boil off gas recovery system

This system consists mainly of two gas recovery compressors together with their associated pipeline. Burckhardt Compression built these two vertical two stage laby compressors in 2001. The compressors are operated at 496 rpm with a maximum flow of 2560 kg/h each, driven by induction motors with a power of 520 kW to recompress boil off gas from the tanks. The capacity is controlled by unloading of suction valves and by switching fixed clearance pockets. The regulation allows the load steps of 100%, 75% (head end clearance pockets open at both stages), 50% (crank end unloaded at both stages), 25% (crank end unloaded, head end clearance pockets open at both stages) and 0%for startup.


During normal operations, a single boil off gas compressor at approximately 50%of its capacity is used to deal with vapour originated as a result of heat in the tanks. Such vapour is then sent to a recondenser, which is able to handle the whole flow of vapour arisen in the terminal, thus keeping tank pressure ur\der the maximum permitted values. Upon LNG carrier unloading operations, a noticeable increase in the gas flow is generated in relation to gas produced during normal operations; therefore, both compressors are used, sending out to the vessel excess gas that has not been absorbed by gas tanks onboard down to the recondenser. These two compressors have a capacity of 2.560 kg/h each. Natural gas propelled by compressors is sent to the recondenser where primary pumps liquefy it. The reliquefier houses an inner cylinder packed with stainless steel pall rings, which forms an annulus with the outer wall of the recondenser. Boil off gas and LNG enter the inner cylinder from the top of the recondenser and are contacted in the packing. The annulus pressure and liquid level are controlled and this maintains a constant pressure at the suction to the sendout pumps. Pressure in the packed bed and annulus are individually controlled by splitting the flow of boil off gas into each one of them. Regulating the LNG flow into the recondenser controls the volume of liquid in the vessel. The bed liquid level varies with pressure and vapour/liquid load on the recondenser. Recondenser pressure is kept by passing a portion of boil off gas from the compressors around the packed bed section of the recondenser. In the event that insufficient boil off gas is available from the compressors, sendout gas
taken upstream of the metering station will be used for recondenser pressure control.

Read the full article from LNG Magazine, January 2009 here.

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