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US 11,353,262 B2Granted
Nitrogen production method and nitrogen production apparatus
AssigneeL'Air Liquide, Societe Anonyme pour l'Etude et l'Exploitation des Procedes Georges Claude
InventorKenji Hirose
Life of this patent
Estimating the term…
Abstract
A portion of feed air is expanded and cooled in front of a main heat exchanger, and is used as cold for precooling the remaining unexpanded feed air inside the main heat exchanger. A portion of the feed air precooled inside the main heat exchanger is removed to outside the main heat exchanger, expanded and cooled, and used as cold to cool the remaining unexpanded precooled feed air inside the main heat exchanger.
Claims9
A method for producing a liquid nitrogen product, the method comprising:
- a precooling step for cooling at least a portion of feed air scrubbed of specified impurities to a first temperature and cooling the precooled feed air;
- a cooling step for cooling at least a first portion of the feed air cooled by the cooling step to a second temperature lower than the first temperature to produce a low-temperature feed air;
- a first expanding step for expanding and cooling a second portion of the feed air cooled by the precooling step to produce a first low-temperature air;
- a second expanding step for expanding and cooling at least a third portion of the feed air to produce a second low-temperature air;
- a first introducing step for expanding and introducing the feed air cooled by the cooling step into a lower section than a first distilling section in a distillation column having the first distilling section;
- a condensing step for condensing at least a portion of the gas inside the distillation column by exchanging heat with an oxygen-rich liquid pooled in a lower section of the distillation column by a condensing section arranged in an upper section of the distillation column;
- a recycled air compressing step for diverting waste gas removed from the condensing section arranged in the upper section of the distillation column and compressing the diverted waste gas in a recycle air compressor;
- a waste gas heat exchange step for exchanging heat between the not diverted waste gas and either the feed air or the precooled feed air;
- a second introducing step for introducing the compressed recycled air compressed by the recycled air compressing step into the lower section of the distillation column than the location of the first distilling section;
- and
- a liquid nitrogen product removing step for removing a liquid nitrogen product from the distillation column,
- wherein the feed air exchanges heat with the first low-temperature air and/or the second low-temperature air in the precooling step and the cooling step,
- wherein the diverted waste gas is sent from the condensing section to the recycled air compressor for the recycled air compressing step without being warmed via heat exchange against the feed air.
10 more elements
A nitrogen production apparatus comprising:
- a main heat exchanger configured to cool a feed air scrubbed of specified impurities;
- a feed air expansion valve configured to expand a low-temperature feed air obtained by cooling feed air in the main heat exchanger to produce a portion of the low-temperature feed air as liquefied feed air;
- and
- a distillation column having a first distilling section whereto the expanded low-temperature feed air is introduced;
- a main feed air supply line configured to supply the feed air through the main heat exchanger to the distillation column;
- a first branch line branching from the main feed air supply line inside the main heat exchanger;
- a first turbine configured to expand a first diverted feed air supplied by the first branch line to produce a first low-temperature air;
- a first low-temperature air introduction line configured to introduce the first low-temperature air to the main heat exchanger;
- a second branch line branching from the main feed air supply line in front of the main heat exchanger;
- a second turbine for expanding a second diverted feed air supplied by the second branch line to produce a second low-temperature air having a lower temperature than the first low-temperature air;
- a second low-temperature air introduction line configured to introduce the second low-temperature air into the main heat exchanger;
- a condensing section arranged in an upper section of the distillation column;
- an oxygen-rich liquid introduction line configured to feed at least a portion of oxygen-rich liquid from a lower section of the distillation column and introducing the oxygen-rich liquid into the condensing section as a coolant;
- a recycled air removal line configured to remove a first portion of waste gas (recycled air) from a location in the condensing section;
- a recycled air compressor configured to compress the first portion of the waste gas supplied by the recycled air removal line;
- a recycled air introduction line configured to introduce the compressed recycled air fed by the recycled air compressor to the distillation column at a lower section of the distillation column than the location of the first distilling section;
- a waste gas line configured to remove a second portion of the waste gas from the condensing section to introduce into the main heat exchanger;
- and
- a liquid nitrogen product removal line configured to remove liquid nitrogen from the distillation column,
- wherein the recycled air compressor is configured to receive the first portion of waste gas from the condensing section without the first portion of waste gas being warmed via heat exchange against the feed air in the main heat exchanger.
17 more elements
Dependencies are inferred from the claim text.