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Process and natural gas compressor

Process and natural gas compressor

Process and natural gas compressor

Process compressors used in the process industry (for example in the liquification, rectification and with chemical reaction of technical gases) have to fulfil demanding requirements in relation to performance and reliability.

Natural gas is a very important resource in the process industry. Its transport in gas pipe lines  or tankers for liquid natural gas , also its storeage underground  requires special natural gas compressors [Cerniak].

Preferably executions  of process compressors  in vertical and horizontal boxer design are being used , which fulfil the requirements of a specific standard  for the oil and gas industry API 618 [6].

The throughput ranges up to 100000 m3/h ( related to standard condition), the discharge pressures up to 100 MPa ( for specific applications up to 360 MPa ).

The driving mechanisms are carried out in various sizes and with different number of cranks. They are designed for minimum deflection and the distance between the cylinders is kept to a minimum. The mean piston velocity goes up to 6 m/sec. The boxer design can achieve a full balance of  mass forces and torque , if the design includes at least two pairs of cranks .

The cylinders are double acting and water cooled. In the low pressure stages big compressor valves with  sufficiently large valve chambers are necessary. This can more easily be done in boxer compressors. The piston rod is sealed by pressure packings. The cylinder is connected to the crank case via a distance piece, which transmits forces and centers the cylinder.

Installations of compressors  with vertical in line cylinders need less space, but have to be fitted with a platform for servicing the cylinders. With balanced opposed piston compressors the coolers are arranged horizontally and parallel to the compressor on the foundation platform. With vertical cylinders, the coolers are arranged externally. In both cases the pulsation dampeners are fitted vertically close to the cylinders.

A special design for non lubricated service is the labyrinth compressor. On the vertically in line arranged cylinders the piston rods have an additional guidance on the lower end of the distance piece. This provides such an excellent guidance, that the pistons can run without touching the liner and with low clearance. Labyrinths on the circumference of the piston and in the packing allow oil free compression with minimum leakage after a short running in period. In order to prevent leakage of the compressed gas to the outside , the crankcase can be sealed  gastight via a double acting sliding ring seal. This design is used for pressures up to 21 MPa.

For the manufacture of  low density polyethylene (ldPE) ethylene has to be compressed to very high pressures. The secondary compressor (Burckhardt Compression) as shown is of the boxer design with 4 pairs of cranks and compresses in two stages from 27 to 320 MPa.

The drive mechanism is equipped with a frame type crosshead, which encloses the forked piston rod and which drives the two coaxially arranged pistons  via additional  round cross heads in the distance pieces. The maximum rod load is 1,86 MN (186 t). A horizontal guidance  is used to take up the vertical force. This guidance is arranged close to the foundation and is strongly dimensioned.

The cylinders are designed from geometrically simple parts with notch free shapes and polished surfaces. The parts are shrunk together, thereby providing compression stresses.