Method and system for providing supplemental refrigeration to an air separation plant

Patent metadata

Field	Value
Publication number	US-10018412-B2
Application number	US-201514935680-A
Country	US
Kind code	B2
Filing date	Nov 9, 2015
Priority date	Nov 9, 2015
Publication date	Jul 10, 2018
Grant date	Jul 10, 2018

Abstract

A system and method for providing supplemental refrigeration to an air separation plant is provided. A closed loop supplemental refrigeration circuit that can be easily retrofitted or added onto an air separation plant that increases the liquid product production capability of the air separation plant. The supplemental refrigeration capacity of the supplemental refrigeration circuit 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 provides the capacity to turn-down liquid product make without shutting down the compressors and turbo-expanders in the supplemental refrigeration circuit.

First claim

What is claimed is:

1. A method of separating air comprising the steps of:
conducting a cryogenic rectification process in an air separation plant in a first mode to produce gaseous products and at least one liquid product stream, the air separation plant comprising a main air compression train configured to compress and purify a feed air stream; a main heat exchanger configured to cool a first portion of the compressed and purified feed air stream to a temperature suitable for the rectification; a turbine based refrigeration circuit configured to further compress, partially cool and expand a second portion of the compressed and purified feed air stream; and a distillation column system configured to rectify the first and second portions of the compressed and purified feed air stream;
operatively coupling a supplemental refrigeration circuit to the air separation plant at a plurality of tie-in points;
wherein a first tie-in point is disposed downstream of the main air compression train and is configured to divert a third portion of the compressed and purified feed air stream; the third portion of the compressed and purified feed air stream being the working fluid for the supplemental refrigeration circuit;
wherein a second tie-in point is disposed downstream of a compressor in the turbine based refrigeration circuit and upstream of the main heat exchanger, the second tie-in point is configured to divert all or a portion of the second portion of the compressed and purified feed air stream to an auxiliary heat exchanger;
wherein a third tie-in point is disposed downstream of the main heat exchanger and upstream of a turbine in the turbine based refrigeration circuit, the third tie-in point is configured to combine the diverted portion of the second portion of the compressed and purified feed air stream from the auxiliary heat exchanger to the turbine based refrigeration circuit upstream of the turbine;
conducting the cryogenic rectification process in the air separation plant in a second mode to produce the gaseous products and the at least one liquid product stream, wherein the liquid product make of the air separation plant operating in the second mode is greater than the liquid product make of the air separation plant operating in the first mode;
wherein the cryogenic rectification process conducted in the second mode further comprises the steps of:
diverting the third portion of the compressed and purified feed air stream as the working fluid to a supplemental refrigeration circuit;
compressing the working fluid in a compressor section within the supplemental refrigeration circuit;
expanding the working fluid in a turbo-expander disposed within the supplemental refrigeration circuit to produce a cooled working fluid;
directing the cooled working fluid to the auxiliary heat exchanger and warming the cooled working fluid in the auxiliary heat exchanger via indirect heat exchange with the diverted portion of the second portion of the compressed and purified feed air stream;
recirculating the warmed working fluid to the compressor section within the supplemental refrigeration circuit after having passed through the auxiliary heat exchanger; and
returning the cooled, the diverted portion of the second portion of the compressed and purified feed air stream exiting the auxiliary heat exchanger to the air separation plant at the third tie-in point to impart a portion of the refrigeration required by the air separation plant to increase the liquid product make.

2. The method of claim 1 further comprising the steps of:
removing a portion of the working fluid in the supplemental refrigeration circuit upstream of the turbo-expander thereby decreasing the refrigeration imparted by the supplemental refrigeration circuit and the production of the at least one liquid product stream or 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 or the adding of the working fluid to the supplemental refrigeration circuit being conducted such that the inlet pressure within the supplemental refrigeration circuit is adjusted commensurate with the desired production of the at least one liquid product stream while the working fluid circulates at a substantially constant volumetric flow rate and the pressure ratio across the compressor section is maintained substantially constant.

3. The method of claim 2 wherein the step of removing a portion of the working fluid in the supplemental refrigeration circuit upstream of the turbo-expander 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.

4. The method of claim 1 further comprising the step of venting a portion of the working fluid downstream of the turbo-expander 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.

5. The method of claim 2 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.

6. The method of claim 2 wherein the working fluid in the supplemental refrigeration circuit is supplied from the compressed and purified air and 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.

7. 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.

8. The method of claim 7 further comprising the step of adjusting turbine nozzles in the turbo-expander to maintain substantially constant volumetric flow rate in the supplemental refrigeration circuit.

9. The method of claim 8 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.

10. An air separation plant comprising:
a main air compression train configured to compress and purify a feed air stream;
a main heat exchanger configured to cool a first portion of the compressed and purified feed air stream to a temperature suitable for the rectification;
a turbine based refrigeration circuit configured to further compress, partially cool and expand a second portion of the compressed and purified feed air stream;
a distillation column system configured to rectify the first and second portions of the compressed and purified feed air stream
a supplemental refrigeration circuit coupled to the air separation plant at a plurality of tie-in points, the suppleme

Assignees

• Sarigiannis Catherine B
• Knight Anna
• Juandi Evelyn
• Zhang Wei
• Rauch Jeremiah J
• Praxair Technology Inc

Inventors

• Sarigiannis Catherine B
• Knight Anna
• Juandi Evelyn
• Zhang Wei
• Rauch Jeremiah J

Classifications

• F25J3/04393

  using multiple or multistage gas work expansion · CPC title

• F25J3/04278

  using external refrigeration units, e.g. closed mechanical or regenerative refrigeration units · CPC title

• F25J3/04224

  Cores associated with a liquefaction or refrigeration cycle · CPC title

• F25J3/04303

  Lachmann expansion, i.e. expanded into oxygen producing or low pressure column · CPC title

• F25J2270/14

  External refrigeration with work-producing gas expansion loop · CPC title