Single column nitrogen rejection unit with side draw heat pump reflux system and method

A system for removing nitrogen from a natural gas fluid feed stream comprising:

• a. a main heat exchanger including a main feed cooling passage, a withdrawn vapor warming passage, a main reflux stream cooling passage, a warm reflux vapor cooling passage, a cold reflux vapor cooling passage and a nitrogen vapor return passage, said main feed cooling passage including an inlet and an outlet, where the inlet of the main feed cooling passage is configured to receive the natural gas fluid feed stream;
• b. a distillation column including a feed inlet, a return vapor outlet, a side vapor outlet port, first, second, and third reflux inlet ports and a bottoms liquid outlet, wherein said side vapor outlet port and said first and second reflux inlet ports are positioned between the feed inlet and the return vapor outlet;
• c. said feed inlet of the distillation column configured to receive a fluid stream from the outlet of the main feed cooling passage of the main heat exchanger, said side vapor outlet port of the distillation column configured to provide vapor to the withdrawn vapor warming passage of the main heat exchanger, said return vapor outlet of the distillation column configured to provide nitrogen vapor to said nitrogen vapor return passage of the main heat exchanger and said first reflux inlet port of the distillation column is in fluid communication with the warm reflux vapor cooling passage of the main heat exchanger;
• d. a reflux compressor configured to receive and compress fluid from the withdrawn vapor warming passage of the main heat exchanger;
• e. a reflux aftercooler configured to receive and cool fluid from the reflux compressor and direct cooled fluid to the main reflux stream cooling passage of the main heat exchanger;
• f. a warm reflux separation device configured to receive fluid from the main reflux stream cooling passage of the main heat exchanger, said warm reflux separation device having a vapor outlet and a liquid outlet, wherein the vapor outlet of the warm reflux separation device is configured to direct fluid to the warm reflux vapor cooling passage of the main heat exchanger and the liquid outlet of the warm reflux separation device is configured to direct fluid to the second reflux inlet port of the distillation column;
• g. a cold reflux separation device having a vapor outlet and a liquid outlet;
• wherein the cold reflux separation device is configured to receive a mixed phase fluid stream from the warm reflux vapor cooling passage of the main heat exchanger, the vapor outlet of the cold reflux separation device is configured to direct a vapor stream to the cold reflux vapor cooling passage, the cold reflux vapor cooling passage is configured to condense a vapor stream and direct a liquid stream to the third reflux inlet port of the distillation column and the liquid outlet of the cold reflux separation device is configured to direct a liquid stream to the first reflux inlet port of the distillation column.

A system for removing nitrogen from a natural gas fluid feed stream comprising:

• a. a main heat exchanger including a main feed cooling passage, a withdrawn vapor warming passage, a main reflux stream cooling passage, a reflux vapor cooling passage, a vapor portion cooling passage and a nitrogen vapor return passage, said main feed cooling passage including an inlet and an outlet, where the inlet of the main feed cooling passage is configured to receive the natural gas fluid feed stream;
• b. a distillation column including a first feed inlet and a second feed inlet, a return vapor outlet, a side vapor outlet port, first and second reflux inlet ports and a bottoms liquid outlet, wherein said side vapor outlet port and said first and second reflux inlet ports are positioned between the feed inlet and the return vapor outlet;
• c. said side vapor outlet port of the distillation column configured to provide vapor to the withdrawn vapor warming passage of the main heat exchanger, said return vapor outlet of the distillation column configured to provide nitrogen vapor to said nitrogen vapor return passage of the main heat exchanger and said first reflux inlet port of the distillation column is in fluid communication with the reflux vapor cooling passage of the main heat exchanger;
• d. a reflux compressor configured to receive fluid from the withdrawn vapor warming passage of the main heat exchanger;
• e. a reflux aftercooler configured to receive and cool fluid from the reflux compressor and direct cooled fluid to the main reflux stream cooling passage of the main heat exchanger;
• f. a reflux separation device configured to receive fluid from the main reflux stream cooling passage of the main heat exchanger, said reflux separation device having a vapor outlet and a liquid outlet, wherein the vapor outlet of the reflux separation device is configured to direct fluid to the reflux vapor cooling passage of the main heat exchanger and the liquid outlet of the reflux separation device is configured to direct fluid to the second reflux inlet port of the distillation column;
• g. an expansion device configured to receive and partially condense a cooled natural gas fluid feed stream from the main feed cooling passage of the main heat exchanger;
• h. a main feed separation device configured to receive a mixed phase stream from the expansion device, said main feed separation device including a vapor outlet and a liquid outlet, wherein the liquid outlet is configured to direct a liquid stream to the first feed inlet of the distillation column;
• i. said vapor portion cooling passage configured to receive and cool a vapor stream from the vapor outlet of the main feed separation device and direct a resulting cooled stream to the second feed inlet of the distillation column;
• wherein said nitrogen vapor return passage and said withdrawn vapor warming passage of the main heat exchanger are configured to cool the main feed cooling passage, the main reflux stream cooling passage and the reflux vapor cooling passage of the main heat exchanger.

A system for removing nitrogen from a natural gas fluid feed stream comprising:

• a. a main heat exchanger including a main feed cooling passage, a withdrawn vapor warming passage, main reflux stream cooling passage, a warm reflux vapor cooling passage, a cold reflux vapor cooling passage and a nitrogen vapor return passage, said main feed cooling passage including an inlet and an outlet, where the inlet of the main feed cooling passage is configured to receive the natural gas fluid feed stream;
• b. a distillation column including a feed inlet, a return vapor outlet, a side vapor outlet port, first, second, and third reflux inlet ports and a bottoms liquid outlet, wherein said side vapor outlet port and said first and second reflux inlet ports are positioned between the feed inlet and the return vapor outlet;
• c. said feed inlet of the distillation column includes a first feed inlet and a second feed inlet and is configured to receive a fluid stream from the outlet of the main feed cooling passage of the main heat exchanger, said side vapor outlet port of the distillation column configured to provide vapor to the withdrawn vapor warming passage of the main heat exchanger, said return vapor outlet of the distillation column configured to provide nitrogen vapor to said nitrogen vapor return passage of the main heat exchanger and said first reflux inlet port of the distillation column is in fluid communication with the warm reflux vapor cooling passage of the main heat exchanger;
• d. a reflux compressor configured to receive fluid from the withdrawn vapor warming passage of the main heat exchanger;
• e. a reflux aftercooler configured to receive and cool fluid from the reflux compressor and direct cooled fluid to the main reflux stream cooling passage of the main heat exchanger;
• f. a warm reflux separation device configured to receive fluid from the main reflux stream cooling passage of the main heat exchanger, said warm reflux separation device having a vapor outlet and a liquid outlet, wherein the vapor outlet of the warm reflux separation device is configured to direct fluid to the warm reflux vapor cooling passage of the main heat exchanger and the liquid outlet of the warm reflux separation device is configured to direct fluid to the second reflux inlet port of the distillation column;
• g. a cold reflux separation device having a vapor outlet and a liquid outlet;
• wherein the cold reflux separation device is configured to receive a mixed phase fluid stream from the warm reflux vapor cooling passage of the main heat exchanger, the vapor outlet of the cold reflux separation device is configured to direct a vapor stream to the cold reflux vapor cooling passage, the cold reflux vapor cooling passage is configured to condense a vapor stream and direct a liquid stream to the third reflux inlet port of the distillation column and the liquid outlet of the cold reflux separation device is configured to direct a liquid stream to the first reflux inlet port of the distillation column;
• wherein said nitrogen vapor return passage and said withdrawn vapor warming passage of the main heat exchanger are configured to cool the main feed cooling passage, the main reflux stream cooling passage, the warm reflux vapor cooling passage and the cold reflux vapor cooling passage of the main heat exchanger.

A method of removing nitrogen from a natural gas fluid feed stream comprising the steps of:

• a. cooling the natural gas fluid feed stream in a main heat exchanger;
• b. directing the cooled natural gas fluid feed stream to a distillation column including the steps of:
• i) separating the cooled natural gas fluid feed stream into a vapor feed stream and a liquid feed stream, and ii) directing the vapor feed stream and the liquid feed stream to the distillation column;
• c. withdrawing vapor from a side of the distillation column;
• d. warming the withdrawn vapor using the main heat exchanger so that refrigeration is provided in the main heat exchanger;
• e. compressing the warmed withdrawn vapor;
• f. cooling and partially condensing the compressed withdrawn vapor to form a first mixed phase reflux stream;
• g. separating the first mixed phase reflux stream into a first liquid reflux stream and a first vapor reflux stream;
• h. directing the first liquid reflux stream to the distillation column;
• i. cooling the first vapor reflux stream so that a second reflux stream is formed;
• j. directing the second reflux stream to the distillation column;
• k. directing a nitrogen vapor return stream from the distillation column to the main heat exchanger;
• l. warming the nitrogen vapor return stream using the main heat exchanger so that refrigeration is provided in the main heat exchanger;
• and
• m. withdrawing liquid from a bottom of the distillation column.

A method of removing nitrogen from a natural gas fluid feed stream comprising the steps of:

• a. cooling the natural gas fluid feed stream in a main heat exchanger;
• b. directing the cooled natural gas fluid feed stream to a distillation column;
• c. withdrawing vapor from a side of the distillation column;
• d. warming the withdrawn vapor using the main heat exchanger so that refrigeration is provided in the main heat exchanger;
• e. compressing the warmed withdrawn vapor;
• f. cooling and partially condensing the compressed withdrawn vapor to form a first mixed phase reflux stream;
• g. separating the first mixed phase reflux stream into a first liquid reflux stream and a first vapor reflux stream;
• h. directing the first liquid reflux stream to the distillation column;
• i. cooling and partially condensing the first vapor reflux stream so that a second mixed phase reflux stream is formed;
• j. directing the second mixed phase reflux stream to the distillation column, including the steps of:
• i) separating the second mixed phase reflux stream to form a second vapor reflux stream and a second liquid reflux stream;
• ii) directing the second vapor reflux stream to the main heat exchanger;
• iii) condensing the second vapor reflux stream in the main heat exchanger so that a third liquid reflux stream is formed;
• iv) directing the second and third liquid reflux streams to the distillation column;
• k. directing a nitrogen vapor return stream from the distillation column to the main heat exchanger;
• l. warming the nitrogen vapor return stream using the main heat exchanger so that refrigeration is provided in the main heat exchanger;
• and
• m. withdrawing liquid from a bottom of the distillation column.