Reciprocating compressor troubleshooting pdf




















Overhaul Services for rotating equipment — the innovative maintenance concept for the digital future of energy. Performance, efficiency, reliability, and low maintenance compressors As a leading supplier of reciprocating compressors, the Dresser-Rand business offers products ranging from medium to high-speed separable units driven by engines or electric motors, to large, slow speed motor driven process reciprocating compressors.

Process Reciprocating Compressors. Process Reciprocating Compressor API Dresser-Rand process reciprocating compressors are available with up to 10 crank throws, as single-throw or balanced-opposed configurations.

High and Medium Speed Reciprocating Compressors. Capacity Control Systems. Variable Capacity Control Systems Most compressors produce more capacity than needed to allow for process control.

Reciprocating Compressor Valves. Reciprocating Compressor Valves Valve performance and reliability is key to compressor performance. Magnum Valve Magnum Hammerhead Valve.

Aftermarket Modifications and Upgrades. Aftermarket Modifications and Upgrades We offer the following state-of-the-art reciprocating compressor upgrades and modernizations to help improve the reliability and availability of your equipment. H2 rich services Reciprocating compressors for hydrogen applications.

We have installed over 2 million horsepower of reciprocating compression in hydrogen rich services. Markets: Process industries Refining H 2 fuel gas boosting H 2 rich fuel with reduced CO 2 emissions from our gas turbines H 2 pipelines H 2 boosting after electrolysis system H 2 storage.

Packager and Parts Distributor Support Data. Visit page. Supply line, Piston — moves through the cylinder in a reciprocating action to compress the gas. Intake valve — to let the air to drawn into the cylinder. Outlet valve — to let air out of the cylinder. Crank shaft — connect to the motor to provide the rotary motion.

Connecting rod — connect the crank and the piston — provide the reciprocating ups and down movement. Assume the compression process being polytropic and the polytropic index is 1. Calculate: a mass of air delivered per minute, and b indicated power. Question 3. Calculate the indicated power required for a free air delivery of 0.

If the compressor is single-acting and has a stroke to bore ratio of 1. If polytropic index is 1. The FAD is 0. The clearance ratio is 0. The expansion 32 process of the cycle follows the law of pV1. For this purpose the induction and free air conditions can be taken as 1. Calculate: a the bore and stroke b the volumetric efficiency c the indicated power d the isothermal efficiency Take the index of compression and re-expansion as 1.

Taking the bore as calculated in Question 3. Calculate also the volumetric efficiency and compare it with that of Question 3.

Answers: 0. It will be brought back to its inlet temperature before induction process. Indicted Mean Effectiv e Pressure. We know that isothermal work done. A two stages, single acting air compressor compresses air to 20bar. The air enters the L. P cylinder at 1bar and 27 o c and leaves it at 4.

The air enters the H. P cylind er is mm diameter and mm stroke. The compressor runs at rpm, taking index of compression and ex pansion in the two cylinders as 1. The indicated power required to run the comp ressor; and 2. The heat rejected in the intercooler per minute.

Indicated power required to run the compressor. We know the sw ept volume of the L. P cylinder.



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