Plant Configurations

Plant Configurations - Low Capital Cost Units

• No heat recovery
• Import steam available for the process
• Low cost feed stock

Plant Configurations - High Export Steam Units

Export steam 100 lbs/1000 SCF of H2 produced



Technical Data:

Feed and Fuel Consumption		Natural Gas	LPG	Naphtha
	MM Btu/h (LHV)	18.09	18.29	18.65
	GJ/h (LHV)	19.09	19.30	19.67
Product Hydrogen	Flow Rate
	NM3/h	1,000	1,000	1,000
	MMSCFD	0.896	0.896	0.896
Pressure
	barg	14	14	14
	psig	203	203	203
Hydrogen Product Purity	Volume %	99.9	99.9	99.9
Utilities
Export Steam
	20 barg. mt/h	1.8	1.7	1.7
	290 psig. t/h	2.0	1.9	1.9
Cooling Water
	m3/h (10 C rise)	12	16	19
	gpm (18 F rise)	53	70	84
Electrical Energy	KW	32	36	34
Demineralized Water
	mt/h	2.4	2.4	2.5
	t/h	2.6	2.6	2.8
Dimensions - Plot Area
	m x m	14 x 20	14 x 20	14 x 20
	ft x ft	46 x 66	46 x 66	46 x 66

Plant Configurations - Low Energy Units (Low Feed & Fuel Consumption)

Energy consumption down to 0.4 MMBTU (LHV) per 1000 SCF of hydrogen produced



Technical Data:

Feed and Fuel Consumption		Natural Gas	LPG	Naphtha
	MM Btu/h (LHV)	14.97	15.16	15.72
	GJ/h (LHV)	15.80	15.99	16.59
Product Hydrogen	Flow Rate
	NM3/h	1,000	1,000	1,000
	MMSCFD	0.896	0.896	0.896
Pressure
	barg	14	14	14
	psig	203	203	203
Hydrogen Product Purity	Volume %	99.9	99.9	99.9
Utilities
Export Steam for Control Only
	20 barg. mt/h	0.3	0.1	0.2
	290 psig. t/h	0.3	>0.1	0.2
Cooling Water
	m3/h (10 C rise)	45	48	51
	gpm (18 F rise)	198	211	225
Electrical Energy	KW	28	32	33
Dimensions - Plot Area
	m x m	14 x 20	14 x 20	14 x 20
	ft x ft	46 x 66	46 x 66	46 x 66

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