Main heat exchanger and a process for cooling a tube side stream

Abstract

A process for cooling a tube side stream in a main heat exchanger is described. The process comprises: a) supplying a first mass flow of a tube side stream to a first zone of individual tubes in the tube bundle; b) supplying a second mass flow of the tube side stream to a second zone of individual tubes in the tube bundle, the second zone being offset from the first zone; c) supplying a refrigerant stream on the shell side for cooling the first and second mass flows; d) removing the evaporated refrigerant stream from the warm end of the main heat exchanger; and, e) adjusting the first mass flow of the tube side stream relative to the second mass flow of the tube side stream to maximise the temperature of the removed evaporated refrigerant stream.

Description

FIELD OF THE INVENTION[0001]The present invention relates to a process for cooling a tube side stream in a main heat exchanger. The present invention further relates to a main heat exchanger for thermally processing a tube side stream. The present invention relates particularly though not exclusively to a process and a main heat exchanger for liquefying a gaseous, methane-rich feed to obtain a liquefied product known as “liquefied natural gas” or “LNG”.Background to the Invention[0002]A typical liquefaction process is described in U.S. Pat. No. 6,272,882 in which the gaseous, methane-rich feed is supplied at elevated pressure to a first tube side of a main heat exchanger at its warm end. The gaseous, methane-rich feed is cooled, liquefied and sub-cooled against evaporating refrigerant to get a liquefied stream. The liquefied stream is removed from the main heat exchanger at its cold end and passed to storage as liquefied product. Evaporated refrigerant is removed from the shell side...

AI Technical Summary

Benefits of technology

[0015]e) adjusting the first mass flow of the tube side stream relative to the second mass flow of the tube side stream to maximise the temperature of the evaporated refrigerant stream removed in step d).

[0021]In one form, the sub-cooled light refrigerant stream removed from the cold end of the cold tube bundle is expanded through a second expansion device to cause a reduction in pressure and produce a reduced pressure light refrigerant stream. In one form, the reduced pressure light refrigerant stream is introduced into the shell side of the main heat exchanger at its cold end, and wherein said reduced pressure light refrigerant stream is allowed to evaporate in the shell side, thereby cooling the fluids in the first and third tube side streams as they travel through the cold tube bundle as well as providing cooling to the fluids in the first, second and third tube side streams as they travel through the warm tube bundle.

[0028]a controller for adjusting the first mass flow of the tube side stream supplied by the first nozzle relative to the second mass flow of the tube side stream supplied by the second nozzle to maximise the temperature of the evaporated refrigerant stream as measured by a temperature sensor.

Problems solved by technology

As spiral-wound heat exchangers become larger to perform increased duties, it becomes increasingly difficult to distribute the shell side fluids evenly.

As a consequence, heat transfer between the shell side and each of the first, second and third tube sides may become uneven across the layers within the bundle.

This uneven distribution of temperature in the shell side fluids leads to unevenness in the temperature in portions of each of the tube side fluids at the cold ends of the bundle from each layer of tubes in the bundle, and for the shell-side fluid exiting at the warm end.

Such pinching causes a drop in efficiency of the main heat exchanger.

Any liquid present represents a significant loss of efficiency and must also be removed to avoid potential damage to the downstream refrigerant compression circuit.

Images