Mode summary for the AA1 example simulation

Purpose

Perform heat and material balance on the system.

N/A

N/A

Furnace

Provide the primary energy source such that the feed is mostly methane.

N/A

N/A

Heater

Apply heat to the high-pressure sCO2. Specify the outlet pressure.

N/A

N/A

Cooler

Cool the low-pressure CO2 before compression.

N/A

N/A

Main Compressor

Compress the cooled sCO2. Specify the outlet pressure.

N/A

N/A

Bypass Compressor

Recompress the bypassed sCO2.

N/A

N/A

Turbine

Expand the high pressure sCO2 and gain work.

N/A

N/A

Header H1

Split the flow between the main and bypass compressors and determine the flow to the CO2 cooler and low-temperature recuperator.

N/A

N/A

High Temperature Recuperator (HTRecup)

Recover the heat from the bypass compressor. Specify the overall heat transfer coefficient and area.

N/A

N/A

Low Temperature Recuperator (LTRecup)

Recover the heat from the main compressor. Specify the overall heat transfer coefficient and area.

N/A

N/A

Header H2

Provide the recompressed CO2 streams back to the high temperature recuperator.

N/A

N/A

ClosedLoop CO2

Set the Fluid Type and the molar flowrate of the sCO2 cyclic loop.

N/A

N/A