Table 6 Overhead heat balance example

From: Refinery Gas Treating Processes

Stream	V or L	°F	lb/h	Btu/lb	MMBtu/h
In
Total O/head	V	218	16,458	615	10.122
Total in					10.122
Out
Prod	V	100	7,506	155.7	1.169
Reflux	L	100	8,952	92.5	0.828
Condenser	By	Diff			8.125
Total out			16,458		10.122

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