Gas Processes Handbook - 82

2019 GAS PROCESSES HANDBOOK
PROCESS CATEGORIES

COMPANY INDEX

Hydrogen, Steam Methane Reforming (cont.)
Economics:
Hydrogen product
Flowrate, Nm³/hr
MMsft3d
Pressure, bara
Purity, mol%
Export steam
Flowrate, tph
Temperature, °C
Pressure, bara
Feed and fuel consumption
Gcal/hr
GJ/hr

Natural
gas

LPG

Naphtha

Refinery
gas

50,000
44.8
25
99.9

50,000
44.8
25
99.9

50,000
44.8
25
99.9

50,000
44.8
25
99.9

31
390
40

28.9
390
40

28.6
390
40

29.2
390
40

177.8
744.4

181.8
761.2

182.9
765.8

175.8
736

3.210
13.440

3.222
13.490

3.072
12.862

55.6
160
850

57.5
165
920

60.6
168
945

53.2
157
780

0.5-1.2

0.4-1.2

0.4-1.2

0.4-1.1

0.9-3.5

1.8-4.3

1.9-4.4

0.7-2.9

Energy consumption (including steam credit)
Gcal/1,000 Nm³ H2
3.070
GJ/1,000 Nm³ H2
12.853
Utilities
Demineralized water, tph
Cooling water, tph
Electrical energy, kW
Design flexibility
Export steam
ton/1,000 Nm³ H2
Fuel consumption
GJ/1,000 Nm³ H2
Investment

Installations: More than 200 new H2 plants have been built around the world for
clients in the refining, chemical and fertilizer industries, with capacities ranging from
less than 1,000 Nm³/hr to more than 100,000 Nm³/hr, and processing all types of
feedstock. Most of these plants have been built on a lump-sum turnkey basis.
Contributor: Linde Aktiengesellschaft

Typically $1.0-1.2 MM per Nm3/h H2,
depending on plant size.

Copyright © 2019 Gulf Energy Information. All rights reserved.



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Gas Processes Handbook

Table of Contents for the Digital Edition of Gas Processes Handbook

Contents
Gas Processes Handbook - 1
Gas Processes Handbook - 2
Gas Processes Handbook - 3
Gas Processes Handbook - Contents
Gas Processes Handbook - 5
Gas Processes Handbook - 6
Gas Processes Handbook - 7
Gas Processes Handbook - 8
Gas Processes Handbook - 9
Gas Processes Handbook - 10
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