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HyGenSys

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Pressurized post combusted Hot Gas Generator exhaust provides all reaction heat input ... Tertiary post combusted reactor exit hot gas offers substantial ... – PowerPoint PPT presentation

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Title: HyGenSys


1
  • - HyGenSys -
  • Gas to Hydrogen and Power Process
  • Facilitates CO2 Capture to Sequestration

Jérôme COLIN Fabrice GIROUDIERE
IFP
2
Outline
  • Backdrop
  • Steam reforming Hydrogen generation
  • Endothermic heat input concept
  • The novel gas-to-hydrogen power process
  • Reactor development for HyGenSys
  • Project status

3
Backdrop
  • CACHET CArbon Capture via Hydrogen Energy
    Technology

Electrical Power production 400 MWe
Co-generation of H2 Ultimate green fuel
SP1WP 1 to 4 technical solution
Natural Gas plentyful ressources high H/C ratio
Capture of 90 of emitted CO2
CO2 Capture cost lt 20 Euros/ton lower cost than
capture from gas combustion flue gas
4
Backdrop
  • SP1-WP1 (advanced SMR HyGenSys)

Work Package leader
SP1-WP1 PARTICIPANTS
5
IFP conceptual HyGenSys integration scheme

H2 Fired Turbine
POWER
H2 PRODUCTION
H2 rich gas
Natural Gas
SP1-WP1 technical solution
CO2 separation unit
Syngas
Compression
CO2
HyGenSys Hydrogen and Power co-generation process
CO2 SEQUESTRATION
6
Outline
  • Backdrop
  • Steam reforming Hydrogen generation
  • Endothermic heat input concept
  • The novel gas-to-hydrogen power process
  • Reactor development for HyGenSys
  • Project status

7
Simplified Reaction Chemistry
Steam Reforming
Endothermic Heat
CH4 H2O 3 H2 CO
Water Gas Shift
Exothermic Heat
CO H2O H2 CO2

Resulting required conversion needs large heat
input to be provided
8
Hydrogen Generation Concept
Steam Reforming
Water Gas Shift
Natural Gas
Synthesis Gas
Raw Hydrogen
First Reaction
Second Reaction
CH4
H2 CO2
Some residual Steam residual CH4 CO
Steam
H2O
9
Outline
  • Backdrop
  • Steam reforming Hydrogen generation
  • Endothermic heat input concept
  • The novel gas-to-hydrogen power process
  • Reactor development for HyGenSys
  • Project status

10
Endothermic Heat Input Concept
Water gas shift
Steam reforming
Natural Gas
Endothermic
Exothermic
Raw Hydrogen
Steam
Hot pressurized gas
Very hot pressurized gas
11
The Heat Source
  • Once through pressurized hot gas from a gas
    generator part of a two-shaft Gas Turbine
  • Other possible gas generator
  • an off-the-shelf Jet engine
  • a gas generator part of an aero-derivative gas
    turbine
  • a purpose made air compressor, combustion chamber
    and power expander

12
Single Shaft Gas Turbine
Atmospheric Exhaust
HP Fuel Gas
Load
Air
Turbine
Axial Compressor
Single shaft Gas Turbine Assembly
13
Split Shaft Gas Turbine
Atmospheric Exhaust
HP Fuel Gas
Load
Air
Compressor Driver Turbine
Axial Compressor
Power Recovery Turbine
Gas Turbine Assembly
14
Split Function Gas Turbine
Atmospheric Exhaust
Still Pressurized Very Hot Exhaust
HP Fuel Gas
Load
Air
Compressor Driver Turbine
Axial Compressor
Power Recovery Turbine
Hot Gas Generator
15
Split Function Gas TurbineEstimated operating
conditions
1 bar 570C
H2 Rich Gas
5.6 bar 860C
17.5 bar 1142C
25.5 bar 200C
18 bar 400C
Load
1 bar 15C
Hot Gas Generator
Power Recovery Turbine
Modified Siemens SGT-700 for Hydrogen firing
16
Outline
  • Backdrop
  • Steam reforming Hydrogen generation
  • Endothermic heat input concept
  • The novel gas-to-hydrogen power process
  • Reactor development for HyGenSys
  • Project status

17
Reaction Heat Flow Concept
Steam Reformer
H2 Rich Gas
Post combustion
Air
Natural Gas Steam
SynGas
Hot Gas Generator Modified Siemens SGT-700
Power recovery Turbine Dresser-Rand E-248
expander

18
Heating Medium Process Flow
H2 rich gas
Stack Gas
Steam
5 bar 630C
HRSG
Power
4.9 bar 760C
5.3 bar 1290C
Secondary combustion After burner
Tertiary combustion
Hot Gas Generator
Power
Tubular Catalytic Reactor / Exchangers
Expander
19
HyGenSys process
Hydrogen rich gas fuel only
CO2 free Flue gas
Air

Hot Gas Generator
Steam
H/E SMR Reactor
HRSG
Steam turbine generator
SH Steam
Expander Generator
BFW
Condensate
20
HyGenSys process
Hydrogen rich gas fuel only
CO2 free Flue gas
Air
Shift Converter

H2 / CO2Separation
Hot Gas Generator
H/E SMR Reactor
Natural Gas
water
CO2 for Sequestration
HRSG
Steam turbine generator
SH Steam
Expander Generator
BFW
Condensate
21
HyGenSys process
Hydrogen rich gas fuel only
CO2 free Flue gas
Air
Shift Converter

H2 / CO2Separation
Hot Gas Generator
H/E SMR Reactor
Natural Gas
water
CO2 for Sequestration
Air
HRSG
Steam turbine generator
SH Steam
Expander Generator
H2 GT Generator
BFW
Condensate
22
HyGenSys Main Features
  • Pressurized post combusted Hot Gas Generator
    exhaust provides all reaction heat input
  • Tertiary post combusted reactor exit hot gas
    offers substantial expansion power generation
  • Hot exhaust offers combined cycle steam power
    generation
  • Maximum power generation from excess hydrogen
    fired GT
  • Flexible ratio of H2 and Power co-generation

23
HyGenSys preliminary performances
  • HyGenSys Integration
  • 4 HyGenSys units in parallel
  • Use of 4 Modified Siemens SGT-700 (Hot Gas
    generators) and 4 Dresser-Rand E-248 (Expanders)
  • 1 Siemens SGT5-4000F modified Hydrogen Fired Gas
    Turbine
  • CO2 separation with Amine unit
  • Resulting performances
  • Net power 617 MWe
  • CO2 Capture ratio 80
  • Overall efficiency 45
  • Total pure H2 production 440 000 Nm3/h

24
Outline
  • Backdrop
  • Steam reforming Hydrogen generation
  • Endothermic heat input concept
  • The novel gas-to-hydrogen power process
  • Reactor development for HyGenSys
  • Project status

25
Reactor development
Hot flue gas
S M R
H2 CO CO2 CH4 H2O
CH4 H2O
Cooled flue gas
26
Reactor specific constrains
  • Reactor challenges and requirements
  • High temperature heat transfer
  • Pressurized vessel
  • High capacity
  • Distribution of feed and flue gas
  • Collection of syngas and cooled flue gas
  • Easy catalyst management
    (loading and unloading)
  • Safety / flexibility in operation

27
Reactor development
  • Conceptual and feasibility study
  • Technology selection
  • Reactor arrangement
  • Integration in HyGenSys
  • Reactor modeling
  • Kinetic
  • Heat transfer

Cold mock-up
Steam Reforming Reactor
  • Material study
  • Creep resistance
  • Metal dusting and carburization
  • Oxidation corrosion

Risk and reliability analysis
Reactor cost estimate
28
Reactor development
  • Technology highlights
  • Original Double pipe / Bayonet tubes concept
  • Convection assisted reformer heating
  • Refractorized and pressurized shell
  • Externalized combustion chamber
  • Reactor specifications overview
  • External diameter 8 m
  • Number of bayonets 300 tubes per reactor

29
Outline
  • Backdrop
  • Steam reforming Hydrogen generation
  • Endothermic heat input concept
  • The novel gas-to-hydrogen power process
  • Reactor development for HyGenSys
  • Project status

30
Project status
  • Completed work
  • Process study
  • CO2 separation technologies assessment ? Amine
    unit
  • HyGenSys integration
  • Reactor development
  • Concepts selection
  • Kinetic and heat transfer model for sizing
  • In progress
  • Process optimization
  • Reactor design validation and cost evaluation
  • Overall HyGenSys technology evaluation

31
Conclusion
  • HyGenSys is a promising process for converting
    gas to hydrogen and power with reduced carbon
    emission
  • It reduces the cost of CO2 capture processes
    thanks to a high level of heat integration
  • Mostly well proven technologies

32
  • THANK YOU FOR YOUR ATTENTION
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