System and method for the production of liquefied natural gas
A system and method for producing liquefied natural gas are provided. The method may include compressing a process stream containing natural gas in a compression assembly to produce a compressed process stream. The method may also include removing non-hydrocarbons from the compressed process stream in a separator, and cooling the compressed process stream with a cooling assembly to thereby produce a cooled, compressed process stream containing natural gas in a supercritical state. The method may further include expanding a first portion and a second portion of the natural gas from the cooled, compressed process stream in a first expansion element and a second expansion element to generate a first refrigeration stream and a second refrigeration stream, respectively. The method may further include cooling the natural gas in the cooled, compressed process stream to a supercritical state with the first and second refrigeration streams to thereby produce the liquefied natural gas.
1. A system for producing liquefied natural gas, comprising
a compressor fluidly coupled with a natural gas source and configured to compress a process stream containing natural gas from the natural gas source to a compressed process stream;
a separator fluidly coupled with the compressor and configured to receive the compressed process stream and at least partially separate water and carbon dioxide from the natural gas in the compressed process stream;
a mechanical chiller in thermal communication with the compressor and configured to cool the natural gas in the compressed process stream to supercritical natural gas;
a turbo-expander fluidly coupled with the compressor and configured to expand a first portion of the supercritical natural gas to generate a first refrigeration stream;
an expansion valve fluidly coupled with the compressor and configured to expand a second portion of the supercritical natural gas to generate a second refrigeration stream;
a first heat exchanger fluidly coupled with the turbo-expander and configured to cool the supercritical natural gas with the first refrigeration stream; and
a second heat exchanger fluidly coupled with the expansion valve and configured cool the supercritical natural gas with the second refrigeration stream.
2. The system of claim 1 , wherein the separator is configured to separate water and carbon dioxide from the natural gas in the compressed process stream at a pressure greater than about 1,000 kPa.
3. The system of claim 1 , further comprising:
an internal combustion engine fluidly coupled with the natural gas source and configured to combust a portion of the natural gas from the natural gas source to generate mechanical energy; and
a generator operatively coupled with the internal combustion engine and configured to convert the mechanical energy to electrical energy to drive the mechanical chiller.
4. The system of claim 1 , further comprising one or more heat exchangers in thermal communication with the compressor and fluidly coupled with the mechanical chiller, the one or more heat exchangers configured to receive a refrigerant from the mechanical chiller to cool the natural gas in the compressed process stream.