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NF-CZ08-OV-1-003-2015 project Study of CCS pilot technologies for coal fired power plants in the Czech Republic VII. Bilateral Workshop/Meeting 11. – 13.

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Presentation on theme: "NF-CZ08-OV-1-003-2015 project Study of CCS pilot technologies for coal fired power plants in the Czech Republic VII. Bilateral Workshop/Meeting 11. – 13."— Presentation transcript:

1 NF-CZ08-OV-1-003-2015 project Study of CCS pilot technologies for coal fired power plants in the Czech Republic VII. Bilateral Workshop/Meeting 11. – 13. 5. 2016, FME CTU in Prague

2 Time schedule Wednesday – 11 th May 2016 (9:30 – 16:00) 9:30 – 12:30 WP3.2 - Economic assessment – Framework, model data, etc. 12:30 – 13:30 Lunch 13:30 – 16:00 WP3.1 - Technical assesment – model design, Framework etc. 17:30 - dinner Thursday – 12 th May 2016 (9:00 – 17:00) 9:00- 10:00 Project Status - finished models, finished data, issues and inconsistencies 10:00-12:00 Review of selected cases (Case matrix and process/chain interfaces ) 12:30-14:00 Lunch – Potrefená Husa 14:00-16:00Work on evaluation of cases ( Running models for all parts of the chain for the different cases and comparing the results) 16:00-17:30 Administration and other issues 18:30 / 19:00Dinner at Břevnov Šenk (monastery incl. little brewery) - http://www.klasternisenk.cz/en/ http://www.klasternisenk.cz/en/ Friday 13 th May 2016 (9:00 – 12:00) 9:00-12:00 Work on evaluation of cases continue (based on outcomes of Thursday’s work 12:00-13:00 Lunch 13:00-15:00Next steps (Who delivers what, when....)

3 Project Goals 1)technical and economical assessment of CCS technologies (based on post- a pre-combustion) integration into IGCC power plant in Czech Republic IGCC. Considered CO2 capture technologies are: Rectisol wash(pre-combustion) Polymeric membranes(pre-combustion) Cryogenic/Low temperature capture(pre-combustion) Ca-Looping (post-combustion) 2)technical and economical study of captured CO2 transport (gas/liquid) to storage in Czech Republic (on-shore) and in North sea (off-shore) transprotu 3)comparison with results from FR-TI/379 project which analysed the integration of oxyfuel and post combustion (ammonia scrubbing) CCS technologies into 250 MWe coal power plant with subcritical parameters in Czech Republic

4 new power plant location: Power plant Prunerov II. area power plant design output => 250 MWe czech lignite focus on using of proven technologies (gasification, gas turbine etc.), except for CO 2 separation technologies. power plant (based case) is based on similar realizations in the world and according to the recommendations derived from the operational experience of IGCC Vresova power plant Input data for design case

5 Basic blok diagrams Oxygen Production Fuel Preparation Gasification Fly Ash Removal Water Gas Shift AGR unit CO 2 Separation Combined Cycle Power Plant Absorption Technology Cryogenic Separation CO 2 Transport H2H2 CO 2 Membrane Separation (addit. activity)

6 Models

7 Steam cycle models for Ca-looping (CVUT x SINTEF) complete all rest models (the end of June 2016) determine the number of cases for optimization (this meeting) first economic results for pre-combustion base cases (the end of May 2016) determine the work schedule for the next two months. Next step/Questions

8 Pre-combustion cases – base cases defined condition for comparison w/o and w CCS is constant fuel consumption (raw lignite mass flow) IGCC w/o CCS (base case 1) IGCC w CCS (85%CCR, 97% CO shift, 95% CO2 purity – membrane, CO2 mixture for transport – in gas form with pressure 110 bar) Rectisol wash (base case 1a) Cryogenic (base case 1b) CO2 membrane (base case 1c) Model - modification or recalculation after CCS technology Gas Turbine unit Steam cycle unit Syngas cooling unit

9 Pre-combustion cases – optimization process Considered configurations (only for one option CCS technologies) Steam cycle (3 cases) Syngas treatment before GT unit (N2 compressor, syngas input temperature, syngas expander) CO shift integration (after or combined with AGR unit) Parameters CCR (60%, 75%, 85%) – only for one option CO shift CO shift (95%, 97%, 99%) – only for one option CCR CO2 purity (85%, 95%, 97%, 99%) – only for one options CO shift and CCR Model - modification or recalculation Gas Turbine unit Steam cycle unit CO2 capture unit Syngas cooling unit CO shift unit

10 Pre-combustion cases – diagram of parameters cases Capture technology (cryogenic, rectisol wash, membrane) CO shift 95% CCR 85% CO shift 97% CCR 60%CCR 75 %CCR 85%CO2 purity 85%CO2 purity 95% CO2 purity 98% CO2 purity 99% CO shift 99% CCR 85%

11 Pre-combustion cases – list of cases No. CaseNo. Sub. I.No. Sub. II.No. Sub.s III. Name case Designation of the Case Technology CO shift conversion factor CO2 capture factorCO2 purity A--- IGCC w/o CCS technology (Base case) A/-/-/- B 95 85- IGCC w CCS technology rectisol, w 95% CO shift conversion factor, w 85% CO2 capture factor (Rectisol separated) B/95/U/- 97 60- IGCC w CCS technology rectisol, w 97% CO shift conversion factor, w 60% CO2 capture factor B/97/L/- in between- IGCC w CCS technology rectisol, w 97% CO shift conversion factor, w „in between" CO2 capture factor B/97/O/- 85- IGCC w CCS technology rectisol, w 97% CO shift conversion factor, w 85/90% CO2 capture factor B/97/U/- 99 85- IGCC w CCS technology rectisol, w 99% CO shift conversion factor, w 85/90% CO2 capture factor (Rectisol separated) B/99/U/- C 95 85- IGCC w CCS technology cryogenic, w 95% CO shift conversion factor, w 85% CO2 capture factor C/95/U/- 97 60- IGCC w CCS technology cryogenic, w 97% CO shift conversion factor, w 60% CO2 capture factor C/97/L/- in between- IGCC w CCS technology cryogenic, w 97% CO shift conversion factor, w „in between" CO2 capture factor C/97/O/- 85- IGCC w CCS technology cryogenic, w 97% CO shift conversion factor, w 85/90% CO2 capture factor C/97/U/- 99 85- IGCC w CCS technology cryogenic, w 99% CO shift conversion factor, w 85/90% CO2 capture factor C/99/U/- D 9585 95 IGCC w CCS technology membrane, w 95% CO shift conversion factor, w 85/90% CO2 capture factor, w CO2 purity - 95% D/95/U/95 97 60% 95 IGCC w CCS technology membrane, w 97% CO shift conversion factor, w 60% CO2 capture factor, w CO2 purity - 95% D/97/L/95 in between 95 IGCC w CCS technology membrane, w 97% CO shift conversion factor, w „between" CO2 capture factor, w CO2 purity - 95% D/97/O/95 85 IGCC w CCS technology membrane, w 97% CO shift conversion factor, w 85/90% CO2 capture factor, w CO2 purity - 85% D/97/U/85 95 IGCC w CCS technology membrane, w 97% CO shift conversion factor, w 85/90% CO2 capture factor, w CO2 purity - 95% D/97/U/95 98 IGCC w CCS technology membrane, w 97% CO shift conversion factor, w 85/90% CO2 capture factor, w CO2 purity - 98% D/97/U/98 99 IGCC w CCS technology membrane, w 97% CO shift conversion factor, w 85/90% CO2 capture factor, w CO2 purity - 99% D/97/U/99 9985 95 IGCC w CCS technology membrane, w 99% CO shift conversion factor, w 85/90% CO2 capture factor, w CO2 purity - 95% D/99/U/95 18 cases maximum

12 Post-combustion cases – optimization process Unit re-design (only for one option CCS technologies) combined SOx and CO2 capture Ca-looping process - ??? Parameters CCR (60%, 75%, 85%) type fuel for calcinator (lignite, syngas)??? O2 purity in calcinator and other - ??? Model - modification or recalculation Steam cycle unit CO2 capture unit ASU unit

13 Post-combustion cases – list of cases No. CaseNo. Sub. I.No. Sub. II.No. Sub.s III. Name case Designation of the Case TechnologyCO shift conversion factor CO2 capture factor CO2 purity A--- IGCC w/o CCS technology (Base case) A/-/-/- E (option 1)- 60%- IGCC w CCS technology Ca-Looping, w 60% CO2 capture factor E/-/L/- in between- IGCC w CCS technology Ca-Looping, w „in between" CO2 capture factor E/-/O/- 85%- IGCC w CCS technology Ca-Looping, w/o CO shift conversion factor, w 85% CO2 capture factor E/-/U/- E (option 2) 85% LF IGCC w CCS technology Ca-Looping, w 85/90% CO2 capture factor, w Lignite as a fuel in calciner E/-/U/LF SF IGCC w CCS technology Ca-Looping, w 85/90% CO2 capture factor, w syngas as a fuel in calciner E/-/U/SF O95 IGCC w CCS technology Ca-Looping, w 85/90% CO2 capture factor, w O2 purity in calciner - 95% E/-/U/O95 O99 IGCC w CCS technology Ca-Looping, w 85/90% CO2 capture factor, w O2 purity in calciner - 99% E/-/U/O99 OE1 IGCC w CCS technology Ca-Looping, w 85/90% CO2 capture factor, w O2 excess ratio in calciner 1 E/-/U/OE1 OE2 IGCC w CCS technology Ca-Looping, w 85/90% CO2 capture factor, w O2 excess ratio in calciner 2 E/-/U/OE2 CO2F1 IGCC w CCS technology Ca-Looping, w 85/90% CO2 capture factor, w CO2 fraction in burner I. E/-/U/CO2F1 CO2F2 IGCC w CCS technology Ca-Looping, w 85/90% CO2 capture factor, w CO2 fraction in burner II. E/-/U/CO2F2 3 -13 cases maximum

14 Transport cases - goals Main goal Comparison of basic transport modes for different capture CO2 (Rectisol, Cryogenic, Membrane). Advantages Disadvantages Selecting the most suitable transport of CO2 for conditions in Czech republic. for on-shore for off-shore

15 Transport cases - list, digram Base case is considered for Rectisol Number of case for calculation (Base case): 8 Case I, Case II and Case II - correspond to different dimensions of pipeline

16 Transport cases - list, digram Comparison with base case(Rectisol) Capture Case I: - Cryogenic Capture Case II: - Membrane Number of case for calculation (Comparison): 8 Total number of case: 16

17 Whole chain analysis cases - list, digram 1 cases for the pre combustion technology (for 1 base case CCS). 1 cases for the post combustion technology Transport in 1 form (gas/liquid) on shore optione

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