초록 ▼

A system and method for air separation using a supplemental refrigeration cycle is provided. A portion of the refrigeration required by the air separation plant to produce a liquid product stream is supplied via a supplemental refrigeration circuit configured to direct a cooled refrigerant produced

A system and method for air separation using a supplemental refrigeration cycle is provided. A portion of the refrigeration required by the air separation plant to produce a liquid product stream is supplied via a supplemental refrigeration circuit configured to direct a cooled refrigerant produced by the turboexpander through the main heat exchanger of the air separation plant. The refrigeration capacity is controlled by removing or adding a portion of the refrigerant in the supplemental refrigeration circuit to adjust the inlet pressure while maintaining a substantially constant volumetric flow rate and substantially constant pressure ratio across the compressor. Removing the refrigerant from the supplemental refrigeration circuit decreases the refrigeration imparted by the supplemental refrigeration circuit and thus decreases the production of the liquid product stream. Adding refrigerant allows for an increase in the refrigeration imparted by the supplemental refrigeration circuit and thus allows for increased production of the liquid product stream.

대표청구항 ▼

1. A method of separating air comprising the steps of: conducting a cryogenic rectification process in an air separation plant comprising a main heat exchanger to cool a compressed and purified feed air stream to a temperature suitable for the rectification of the feed air stream and a distillation

1. A method of separating air comprising the steps of: conducting a cryogenic rectification process in an air separation plant comprising a main heat exchanger to cool a compressed and purified feed air stream to a temperature suitable for the rectification of the feed air stream and a distillation column system configured to rectify the compressed, purified and cooled air to produce at least one liquid product stream;providing a portion of the refrigeration required by the air separation plant to produce the at least one liquid product stream via a supplemental refrigeration circuit, the supplemental refrigeration circuit comprising a working fluid comprising a portion of the compressed and purified feed air stream; a compressor section configured to compress the working fluid; and a turboexpander section configured to expand the working fluid to generate cooled working fluid, the supplemental refrigeration circuit configured to direct the cooled working fluid through the main heat exchanger;warming the cooled working fluid in the main heat exchanger to impart the portion of the refrigeration required by the air separation plant;recirculating the working fluid to the compressor section of the supplemental refrigeration circuit after having passed through the main heat exchanger; andremoving a portion of the working fluid in the supplemental refrigeration circuit upstream of the turboexpander section thereby decreasing the refrigeration imparted by the supplemental refrigeration circuit and the production of the at least one liquid product stream and adding working fluid to the supplemental refrigeration circuit upstream of the compressor section thereby increasing the refrigeration imparted by the supplemental refrigeration circuit and the production of the at least one liquid product stream;wherein the removal of the working fluid from the supplemental refrigeration circuit and the adding of the working fluid to the supplemental refrigeration circuit being conducted in a manner such that the inlet pressure within the supplemental refrigeration circuit is adjusted commensurate with the desired production of the liquid product stream; the working fluid circulates within the supplemental refrigeration circuit at a substantially constant volumetric flow rate; and the pressure ratio across the compressor section is maintained substantially constant. 2. The method of claim 1 wherein the step of removing a portion of the working fluid in the supplemental refrigeration circuit upstream of the turboexpander section further comprises venting a portion of the working fluid to maintain the working fluid in the supplemental refrigeration circuit at or below a prescribed maximum pressure. 3. The method of claim 1 further comprising the step of venting a portion of the working fluid downstream of the turboexpander section of the supplemental refrigeration circuit to maintain the working fluid in the supplemental refrigeration circuit at or below a prescribed maximum pressure and to maintain the cooled working fluid directed to the main heat exchanger at or below a prescribed maximum temperature. 4. The method of claim 1 wherein the step of adding working fluid to the supplemental refrigeration circuit upstream of the compressor section further comprises adding a flow of make-up working fluid to the supplemental refrigeration circuit to maintain the inlet pressure to the compressor section at or above a prescribed minimum pressure. 5. The method of claim 1 wherein the step of adding working fluid to the supplemental refrigeration circuit upstream of the compressor section further comprises modulating the supply of the working fluid charge to the supplemental refrigeration circuit to adjust the inlet pressure of the compressor section. 6. The method of claim 1 further comprising the step of adjusting compressor guidevanes in the compressor section to maintain the substantially constant pressure ratio across the compressor section. 7. The method of claim 6 further comprising the step of adjusting turbine nozzles in the turboexpander section to maintain substantially constant volumetric flow rate in the supplemental refrigeration circuit. 8. The method of claim 7 further comprising the step of operatively controlling the amount of supplemental refrigeration required by the air separation plant to produce the at least one liquid product stream by controlling the removal of working fluid, the addition of working fluid, the adjusting of compressor guidevanes, and the adjusting of turbine nozzles via a controller to maintain a substantially constant pressure ratio across the compressor section and substantially constant volumetric flow rate in the supplemental refrigeration circuit. 9. The method of claim 1 wherein the step of conducting the cryogenic rectification process further comprises the steps of: compressing and purifying an air feed stream to produce the compressed and purified feed air stream;dividing the compressed and purified feed air stream into a first compressed air stream and a second compressed air stream;further compressing, cooling, and expanding the first compressed air stream and second compressed air stream to form a first intake liquid stream and a second intake stream, respectively, and introducing the first intake liquid stream and a second intake stream to the distillation column system; andfractionally distilling the intake streams into their component parts in the distillation column system to produce a plurality of product and waste streams, including the at least one liquid product stream.