Office of Fossil Energy Overview of Supercritical Carbon Dioxide Technology Effort

Similar documents
Supercritical CO 2 Brayton Power Cycles Potential & Challenges

TECHNICAL AND ECONOMIC EVALUATION OF SUPERCRITICAL OXY-COMBUSTION FOR POWER GENERATION

Power cycle development

Highlights of DOE Nuclear Reactor Technologies Program

Challenges in Designing Fuel-Fired sco2 Heaters for Closed sco2 Brayton Cycle Power Plants

Overview of Supercritical Carbon Dioxide Based Power Cycles for Stationary Power Generation

Application of an Integrally Geared Compander to an sco 2 Recompression Brayton Cycle

Analysis of a Directly Heated Oxyfuel Supercritical Power Generation System

DEVELOPMENT OF A 1 MWE SUPERCRITICAL CO 2 BRAYTON CYCLE TEST LOOP

NET Power. Truly Clean, Cheaper Energy. California Energy Commission CO 2 Capture Technology Workshop. April 16, April NET Power

Chapter 9: Vapor Power Systems

Conception of a Pulverized Coal Fired Power Plant with Carbon Capture around a Supercritical Carbon Dioxide Brayton Cycle

Oxy Fuel Turbine Technology

Oxy Fuel Turbine Technology

BLUE OPTION White space is filled with one or more photos

Advanced Coal Technology 101

GE Global Research Rahul Bidkar Doug Hofer Andrew Mann Max Peter Rajkeshar Singh Edip Sevincer Azam Thatte

Design Optimisation of the Graz Cycle Prototype Plant

PowerEnergy

Technology Adaptation In Power Generation

High-efficiency low LCOE combined cycles for sour gas oxy-combustion with CO[subscript 2] capture

Supercritical CO2 Brayton Cycles and Their Application as a Bottoming Cycle. Grant Kimzey UTSR Intern Project Summary Webcast September 7, 2012

Air Separation Unit for Oxy-Coal Combustion Systems

IV International Seminar on ORC Power Systems. del Duomo di Milano

CSP and Natural Gas Hybrids

Public Workshops on Carbon Capture and Sequestration

Development of Integrated Flexi-Burn Dual Oxidant CFB Power Plant

Sustainable Energy Mod.1: Fuel Cells & Distributed Generation Systems

Installation of the Supercritical CO 2 Compressor Performance Test Loop as a First Phase of the SCIEL facility

Stationary Combustion Systems Chapter 6

Thermo-Economic Analysis of Four sco2 Waste Heat Recovery Power Systems

CCUS Major Demonstrations Program Overview

MULTI-OBJECTIVE OPTIMIZATION ON SUPERCRITICAL CO 2 RECOMPRESSION BRAYTON CYCLE USING KRIGING SURROGATE MODEL

Potential of Allam cycle with natural gas to reduce carbon dioxide emission in India

Economic analysis of SCO2 cycles with PCHE Recuperator design optimisation

Advanced Coal Technologies for Power Generation

Advanced Hydrogen and CO 2 Capture Technology for Sour Syngas

Concentrating Solar Power: Current Cost and Future Directions

Sandhya Eswaran, Song Wu, Robert Nicolo Hitachi Power Systems America, Ltd. 645 Martinsville Road, Basking Ridge, NJ 07920

Ion Transport Membrane (ITM) Technology for Lower-Cost Oxygen Production

Chapter 8. Vapor Power Systems

Electricity Generation

The Zero Emission Power Plant Concept

Oxy-coal combustion pressurized technology: Status and developments

Decentralized Biomass Power Production

J-POWER s CCT Activities

The Future of IGCC Technology CCPC-EPRI IGCC Roadmap Results

A Further Step Towards a Graz Cycle Power Plant for CO 2 Capture

Consider a simple ideal Rankine cycle with fixed turbine inlet conditions. What is the effect of lowering the condenser pressure on

Chapter 10 VAPOR AND COMBINED POWER CYCLES

DEVELOPMENT OF HITACHI OXY-COMBUSTION TECHNOLOGY WITH NEW TYPES OF BURNER AND FLUE GAS RE-CIRCULATION SYSTEM

Capture-Ready Coal Plants - Options, Technologies and Economics

Future of Coal in America Update on CO 2 Capture & Storage Project at AEP s Mountaineer Plant

VALLIAMMAI ENGINEERING COLLEGE

Thermo-Economic Analysis of Four sco2 Waste Heat Recovery Power Systems

Reforming Natural Gas for CO 2 pre-combustion capture in Combined Cycle power plant

CO2 Capture with Foster Wheeler s Flexi-burn TM CFB Technology

Andy Schroder Mark Turner University of Cincinnati, Cincinnati, OH, 45221, U.S.A. Abstract

DOE Perspective on Advanced Energy Materials

Tutorial: Fundamentals of Supercritical CO 2

Technology Development Partner

Gas turbines have been used for electricity generation. Gas turbines are ideal for this application as they can be started and stopped quickly.

- The Osaki CoolGen Project -

Advanced Centrifugal Compression and Pumping for CO 2 Applications

Technical and Economic Evaluation of a 70 MWe Biomass IGCC Using Emery Energy s Gasification Technology

S-CO 2 Brayton Loop Transient Modeling

Testing and Feasibility Study of an Indirectly Heated Fluidized-Bed Coal Gasifier

Supercritical CO2 Brayton Cycles for Solar- Thermal Energy

Status of CCUS in the United States. Jarad Daniels. Office of Fossil Energy. Acting Deputy Assistant Secretary for Clean Coal and Carbon Management

Gasification: A Key Technology Platform for Western Canada s Coal and Oil Sands Industries

The way forward for CCS in Poland

USEA Briefing Washington DC. Neil Kern, July 21, 2016

Status and Outlook for CO 2 Capture Systems

MIT Carbon Sequestration Forum VII Pathways to Lower Capture Costs

Overview of CO2 Capture Technologies, System Integration, and Costs

Module 2: Conventional Power Generation I

Gas turbine power plant. Contacts: Mail: Web:

Development of a Flexible Modeling Tool for Predicting Optimal Off-Design Performance of Simple and Recompression Brayton Cycles

SOME ENERGY-EFFICIENT TECHNOLOGIES IN JAPAN

Creating the Future of Coal-Fired Power Generation

Cost and Performance Baseline for Fossil Energy Plants

Canadian Clean Power Coalition: Clean Coal-Fired Power Plant Technology To Address Climate Change Concerns

S-CO 2 Brayton Loop Transient Modeling

Applied Thermodynamics - II

Chapter 1 STEAM CYCLES

COAL-FIRED POWER PLANT PLANNING ASSUMPTIONS

Overview of learning curves. Application to power plants Application to emission control technologies Implications for future CCS costs

Siemens Carbon Capture Technology

2. TECHNICAL DESCRIPTION OF THE PROJECT

Advanced Supercritical Carbon Dioxide Power Cycle Configurations for Use in Concentrating Solar Power Systems

CO 2 Capture from Natural Gas Combined Cycles

A Comparative Study of Heat Rejection Systems for sco 2 Power Cycles

Techno-Economic Assessment of Oxy-Combustion Turbine Power Plants with CO 2 Capture

CANMET Energy Technology Centre R&D Oxy-Fuel Combustion for CO 2 Capture

Available online at ScienceDirect. Energy Procedia 114 (2017 )

Rankine (steam) Cycle Cooling Options

Brayton Cycle. Introduction. Definitions. Reading Problems , 9-105, 9-131

Technology and Prospect of Process Heat Application of HTR(High temperature gas cooled reactor) Applications in Oil Refining Industry

Feature: New Project Development Using Innovative Technology

Fundamental Investigation Of Whole-Life Power Plant Performance For Enhanced Geothermal Systems

Transcription:

Office of Fossil Energy Overview of Supercritical Carbon Dioxide Technology Effort 5 th International sco 2 Power Cycles Symposium March 29, 2016

What we do

Supercritical Pulverized Coal Power Plant Summary Performance 550 GROSS POWER (MW) (580) 27 3 0 0 Gross Power (MW) with Capture (642) 4 35 16 36 550 Balance of Plant Flue Gas Cleanup CO2 Caputre CO2 Compression Net Power (MW) 3

Supercritical Pulverized Coal Power Plant Summary Performance TOTAL PLANT COST (947) TOTAL PLANT COST (1,890) 167 0 0 98 947 484 1111 197 Millions 2011$ Base Plant CO2 Capture Gas Cleanup CO2 Compression 4

The Challenge of Carbon Capture 5

Supercritical CO2 Cycle Has Broad Applicability Supercritical CO 2 Brayton Cycle 5 Solar SunShot Power Cycle Turbine Compressors Alternator 1 Waste Heat Chiller Nuclear 6 3 2 Space Solar Electric Propulsion Fossil Sequestration Ready CO 2 4 7 8 HT RecupLT Recup Geothermal The long-term vision is widespread commercial deployment of a transformational technology 6

Fossil Energy Supercritical CO2 Power Cycles Base Program SCO2 Cycles for FE Applications Indirectly-heated cycle Applicable to advanced combustion boilers Incumbent to beat: USC/AUSC boilers Thermal eff. > 50% possible High fluid density, low pressure ratio yields compact turbomachinery Ideally suited to constant temp heat source Adaptable for dry cooling Directly-heated cycle Applicable to IGCC and NGCC Incumbent to beat: Adv. F- or H-class NGCC w/ post CCS Compatible w/ RD&D from indirect cycle Fuel flexible: coal syngas or NG 100 % CO 2 capture at storage pressure Water producer

FE SCO2 Power Cycles Program - Summary Benefits of Supercritical CO2 Based Power Cycles Higher efficiency Lower emissions per MWhr and positively affects COE calculation Indirect (STEP): ~ 3 % pts greater than steam at the same temperature Direct: Depends on TIT, need to beat F / H -class NGCC with CCS Lower Cost and Small Footprint with new high temperature materials and adv. manufacturing Fuel/energy source flexibility Water producer direct fire configuration DOE FE SCO2 Power Cycles Program - two thrusts: DOE SCO2 Crosscut Initiative (STEP Indirectly heated SCO2 Brayton cycle) FE SCO2 Power Cycles Base Program (indirectly & directly heated cycles for FE applications) DOE SCO2 Crosscut Initiative (STEP) Collaboration between DOE Offices (FE, NE, and EERE CSP & Geothermal) Mission: Address technical issues, reduce risks, and mature technology Objective / goal: Design, build, and test 10 MWe pilot facility (STEP) Major Crosscut procurement actions: Advanced recuperator development (FE FOA: $ 10 M in FY 2015) Cost and technical approach for STEP (NE RFP: 3 awards) Design, build & operate STEP facility (FE FOA Released ~ $ 100 M total value)

FE SCO2 Power Cycles Program R&D FE SCO2 Power Cycles Base Program R&D work specific to FE heat sources (funding from: AT, ACS and CCR&D) Additional R&D projects on critical components, analysis, simulation, and fundamental properties. Turbomachinery Recuperators Oxy-fuel Combustion SCO2 Heater Integration Materials & Fundamentals Systems Analysis

STEP Activities in Fossil Energy FE 2016 FOA: Design & Build STEP Facility FY2016 FE STEP FOA $ 80 M government value (ceiling) with 20 % cost share FOA issued March 2016 Cooperative agreement to be awarded August / September 2016 Project Objective: Design and build STEP test facility 10 MWe pilot plant Indirect-fired recompression Brayton cycle STEP Test Facility Goals Show potential for lower cost of electricity (COE) in relevant applications Demonstrate operability of cycle Verify component performance

FE SCO2 Base Program: Project Activities Technical Challenges - Turbomachinery Turbomachinery must be designed to address specific requirements of SCO2 power cycle to operate at higher temperatures with greater power density, enabling increased efficiencies over steam-based cycles. Technical Challenges Designs for high gas density, high power density and real gas effects of CO 2 near the critical point Identification of materials/coatings having compatibility with SCO2 at temperatures/pressures of the turbomachinery operation Designs for higher temperatures of direct-fired cycle Bearings and low-leakage seals with long performance lives under high temperature/pressure conditions Pressure containment Thermal management

FE Base Program: Project Activities Oxy-fuel Combustion/Turbomachinery Technical Challenges Achieving the additional efficiency improvements operating at higher temperatures of direct-fired power cycle require unique designs of oxy-fuel combustors. Technical Challenges Development of high inlet temperature combustor with oxy fuel and CO 2 diluent Injector designs Determine optimal fuel and oxygen injection locations Complete combustion Minimize hot spots and wall temperatures Understand combustion kinetics and dynamics at high temperature/pressure conditions with syngas or natural gas and CO 2 diluent Minimal validation data and kinetic models at operating conditions

FE Base Program: Project Activities Recuperators for Power Cycles Technical Challenges Recuperation of heat from low pressure fluid at turbine exit to the high pressure fluid upstream of primary heat source is vital to attaining efficiency improvements of the power cycle. Technical Challenges Low cost, compact heat exchanger designs High surface area for heat transfer to provide required heat duty (surface area density > 700 m 2 /m 3 ) Identification of materials compatible with at temperatures (>700 C) and pressures (up to 30 MPa) of the cycle Designs for high temperatures and high pressures as well as high pressure differentials (up to 30 MPa) between streams Mechanical stability Pressure containment Minimal leakage Identification of scalable manufacturing techniques Recuperator design requires optimization of pressure drop, heat transfer coefficient, and temperature difference (approach temperature) Balance capital cost versus efficiency

FE Base Program: Project Activities Heater Integration Technical Challenges Substitution of indirectly-heated power cycles for traditional supercritical steam based power cycles has potential for improved efficiency. Technical Challenges Integrate the power cycle with fossil fuel heat source. Consider both greenfield and retrofit applications. Develop boiler design, including heat exchanger, to deliver higher temperature required for the working fluid. Heater surface (boiler) cost challenge due to high temperature and pressure conditions

FE Base Program: Project Activities Systems Modeling / Analysis Technical Challenges Indirect power cycles have the potential for efficiency improvement over steam Rankine cycles, and direct cycles promise 40+% thermal efficiency with carbon capture and storage Technical Challenges Translation of cycle efficiency benefits to plant efficiency improvement Identification of cycle conditions for optimized cycle performance, cost, and operability Lack of cost estimates for most cycle equipment at commercial scales hinders COE evaluations Efficient integration of power cycles into fossil-fueled heat sources with widely varying flue gas temperatures Efficient handling of significantly increased mass flows relative to comparably-sized steam Rankine power cycles Uncertainties in combustion and pollutant cleanup processes in directfired systems Optimization of component cost vs. performance to minimize overall plant COE