EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, 2008 1 L. Mansani WP1.2 EFIT and XP-ADS Data.

Slides:



Advertisements
Similar presentations
A case history of CFD support to Accelerator Driven System plant
Advertisements

(1) Die Kooperation von Forschungszentrum Karlsruhe GmbH und Universität Karlsruhe (TH) 0 | Transient Analysis for the EFIT 3-Zone Core P. Liu, X.-N. Chen,
Forschungszentrum Karlsruhe Technik und Umwelt IRS /FzK W.M.SchikorrEUROTRANS WP1.5 Safety Meeting : Lyon, Oct EFIT (PB) - Design and Preliminary.
Forschungszentrum Karlsruhe Technik und Umwelt IRS /FzK W.M.SchikorrEUROTRANS WP1.5 Safety Meeting : Madrid, Nov EFIT Design and Transient.
DM1 – WP1.5 meeting Stockholm, May 22-23, First safety approach of the DHR system of XT-ADS B. Arien.
Preliminary T/H Analyses for EFIT-MgO/Pb Reactor Design WP1.5 Progress Meeting KTH / Stockholm, May 22-23, 2007 G. Bandini, P. Meloni, M. Polidori Italian.
EUROTRANS – DM1 RELAP5 Model Evaluation with SIMMER-III Code and Preliminary Transient Analysis for EFIT Reactor WP5.1 Progress Meeting KTH / Stockholm,
Transmutation and ADS Safety EUROTRANS WP1.5 Meeting, Nov 27-28, Karlsruhe Simulation of EFIT Steam Generator Tube Rupture Accident (U-10) M. Flad, S.
1 Single-cycle mixed-fluid LNG (PRICO) process Part I: Optimal design Sigurd Skogestad & Jørgen Bauck Jensen Quatar, January 2009.
Forschungszentrum Karlsruhe Technik und Umwelt IRS /FzK W.M.SchikorrEUROTRANS WP1.5 Safety Meeting : Lyon, Oct Temperature Limits for XT-ADS.
EUROTRANS WP 1.5 Meeting FZK – Karlsruhe, November 27-28, 2008 FPN-FISNUC / Bologna EUROTRANS – DM1 EFIT Transients Analysis with RELAP5, SIMMER-III and.
AREVA NP EUROTRANS WP1.5 Technical Meeting Task – ETD Safety approach Safety approach for EFIT: Deliverable 1.21 Lyon, October Sophie.
Framatome ANP IP-EUROTRANS Meeting WP 1.5 Progress in safety approach development TEE, March Sophie EHSTER.
Transmutation and ADS Safety Forschungszentrum Karlsruhe in der Helmholtz-Gemeinschaft Transient Analysis for EFIT (ENEA 384MWth 3-Zone core) Safety and.
May 22nd & 23rd 2007 Stockholm EUROTRANS: WP 1.5 Task Containment Assessment IP-EUROTRANS DOMAIN 1 Design WP 1.5 Safety Assessment of the Transmutation.
EUROTRANS – DM1 Preliminary Transient Analysis for EFIT with RELAP5 and RELAP/PARCS Codes WP5.1 Progress Meeting Empresarios Agrupados - Madrid, November.
EUROTRANS: WP1.5 Technical meeting, Karlsruhe, November 27 – 28, XT-ADS DHR Conceptual Design L. Mansani
AREVA NP EUROTRANS WP1.5 Technical Meeting Task – ETD Safety approach Safety approach for XT-ADS: Deliverable 1.20 Lyon, October Sophie.
ENGINEERING PROJECT PROPOSAL MASTER OF ENGINEERING IN MECHANICAL ENGINEERING DAN FLAHIVE Analytical Method to Predict Primary Side Steam Generator Pressure.
1 Safety studies for MYRRHA B. Arien, S. Heusdains, H. Aït Abderrahim on behalf of the MYRRHA Team and Support IP-Eurotrans Workshop DM1-WP1.5Brussels,
EUROTRANS - Helium cooled EFIT Probabilistic assessment of different DHR designs Karlsruhe, November Sophie EHSTER, Laurent VINCON.
Forschungszentrum Karlsruhe Technik und Umwelt IRS /FzK W.M.SchikorrEUROTRANS WP1.5 Safety Meeting : Karlsruhe, Nov 27-28, EFIT-Pb Transient Analysis.
Bologna on 28 May 2008 – IP EUROTRANS WP1.51 IE - Institute for Energy Petten - The Netherlands
Forschungszentrum Karlsruhe Technik und Umwelt IRS /FzK W.M.SchikorrEUROTRANS WP1.5 Safety Meeting : Madrid, Nov XT-ADS Transient Analysis.
WP 1.5 Progress Meeting ENEA – Bologna, Italy, May 28-30, 2008 FPN-FISNUC / Bologna EUROTRANS – DM1 Analysis of EFIT Unprotected Accidental Transients.
CHW Optimization Case Studies
KIT – University of the State of Baden-Wuerttemberg and National Research Center of the Helmholtz Association Institute for Nuclear and Energy Technologies.
Nuclear Fundamentals Part II Harnessing the Power of the Atom.
Specifying and Sizing Control Valves A design equation used for sizing control valves relates valve lift to the actual flow rate q by means of the valve.
Lesson 7 FIRST LAW OF THERMODYNAMICS STATE the First Law of Thermodynamics. Using the First Law of Thermodynamics, ANALYZE an open system including all.
Investigation into the Viability of a Passively Active Decay Heat Removal System In ALLEGRO Laura Carroll, Graduate Physicist Physics & Licensing Team,
Chapter 4.3: Compact Heat Exchangers
Norwegian Building Research Institute P.O.Box 123 Blindern Forskningsveien 3B 0314 Oslo Norway   Contact persons: J.T. Brunsell.
Fluid Mechanics and Applications MECN 3110
Thermal hydraulic analysis of ALFRED by RELAP5 code & by SIMMER code G. Barone, N. Forgione, A. Pesetti, R. Lo Frano CIRTEN Consorzio Interuniversitario.
1 ME421 Heat Exchanger Design Drain Water Heat Recovery System Project Presentation Group #5.
Analyses of representative DEC events of the ETDR
LEADER WP3 Conceptual Design Status KIT Town Office Ostendorfhaus Weberstraße 5, Karlsruhe, Luigi Mansani
CHAPTER 5: Mass and Energy Analysis of Control Volumes
ALFRED System Configuration Luigi Mansani
ME421 Heat Exchanger Design
Chapter 4 Control Volume Analysis Using Energy. Learning Outcomes ►Distinguish between steady-state and transient analysis, ►Distinguishing between mass.
Development of a RELAP5-3D thermal-hydraulic model for a Gas Cooled Fast Reactor D. Castelliti, C. Parisi, G. M. Galassi, N. Cerullo (San Piero A Grado.
ALFRED and ELFR design overview Technical Workshop to Review Safety and Design Aspects of European LFR Demonstrator (ALFRED), European LFR Industrial Plant.
EUROTRANS – DM1 ENEA Activities on EFIT Safety Analysis ENEA – FIS/NUC Bologna - Italy WP5.1 Progress Meeting Tractebel / Brussels, March 17, 2006 G. Bandini,
IAEA Meeting on INPRO Collaborative Project “Performance Assessment of Passive Gaseous Provisions (PGAP)” December, 2011, Vienna A.K. Nayak, PhD.
1 Kaspar Kööp, Marti Jeltsov Division of Nuclear Power Safety Royal Institute of Technology (KTH) Stockholm, Sweden LEADER 4 th WP5 MEETING, Karlsruhe.
Chapter 4 Control Volume Analysis Using Energy (continued)
1 ME421 Heat Exchanger Design Drain Water Heat Recovery System Project Presentation Group #5.
Full Scale Thermosyphon Design Parameters and Technical Description Jose Botelho Direito EN/CV/DC 19 November, th Thermosyphon Workshop.
LEADER WP3 Conceptual Design Status KIT Campus North, Karlsruhe, Luigi Mansani
Page 1 Petten 27 – Feb ALFRED and ELFR Secondary System and Plant Layout.
ME 414 Thermal&Fluid Systems Design Heat Exchanger Design ME 414 Thermal / Fluid System Design William Donelson Josh Fosso Laurie Klank Jonathan Moore.
Analysis of Mingled Shell-side stream P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Splitting of A Circuitous Flow into Simple.
CHAPTER 4 The First Law of Thermodynamics for Control Volumes.
Lecture Objectives: Answer question related to Project 1 Finish with thermal storage systems Learn about plumbing systems.
Lecture Objectives: Learn about Pumps and System Curves.
Italian National Agency for New Technologies, Energy and Environment Advanced Physics Technology Division Via Martiri di Monte Sole 4, Bologna, Italy.
EUROTRANS – DM1 Preliminary Transient Analysis for EFIT Design WP5.1 Progress Meeting AREVA / Lyon, October 10-11, 2006 G. Bandini, P. Meloni, M. Polidori.
Lecture Objectives: Plumbing Pumps Hydronic distribution systems
Status of the SAD Project V. Shvetsov, FLNP. SAD Project Objectives Coupling all major components of ADS; Core design, safety assessment, licensing; k.
Vectors.
Date of download: 12/24/2017 Copyright © ASME. All rights reserved.
Plate Heat Exchanger (PHE)
MINI 1A iAquaMax™ Kidney / water removal system
1A iAquaMax™ Kidney / water removal system
Lecture Objectives: Learn about plumbing system and pumps
Lecture Objectives: Learn about plumbing system and pumps
50 m EML3015C Thermal-Fluid I Fall 2000 Homework 4
System Curve Example Design Condition 20 ft.w.c. required each way to deliver design flow to and from the headers at the loads Distribution Pump Bell.
Presentation transcript:

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, L. Mansani WP1.2 EFIT and XP-ADS Data

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, Reference Documents EFIT D1.24 Main Component Functional Sizing of the EFIT (under review to make consistent with D1.26 and to include primary system pressure losses, Lead volume, primary and target pumps characteristics, DHR 1 & DHR 2, CFX evaluation, etc) D1.26 Main Component Assembly Drawings of EFIT (issued) XT-ADS D1.27 & D1.28 Description and functional sizing of the Main Components of the Reference Design of the XT-ADS (Draft) Main Component Assembly Drawings of EFIT (Draft)

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, P- head 1.37 bar SG ΔPsg 0.4 bar mfr 4500 kg/s ΔPp 0.27 bar mfr 9000 kg/s ΔPc = 0.7bar mfr = kg/s ΔPc-in = 0.3 bar ΔPc-out = 0.1 bar ΔP-rods = 0.2bar ΔPc-grids = 0.1 bar ΔPsg + ΔPc = P-head – ΔPp ΔPsg Pressure Drops and Free Levels in the EFIT Primary System Primary coolant flow rates [Kg/s] total: across the core - fuel assemblies: fuel assemblies by-pass: dummy assemblies: 550 across the HX of the Target Unit: 1500 across each pump: 9000 across each SG: 4500 Δ Pc: fuel assemblies pressure drop ΔPp: pump duct pressure drop, with pump working ΔPsg: SG pressure drop P-head: head of the pump SGU Midplane Core Midplane Pump ΔPp= 0.5 ξρv 2 ξ=2.2 pump in operation ξ=3.7 pump free ξ= 5.6 pump locked

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, SG v = 0.6 m/s Lead Mass Distribution and Average Velocities in the EFIT Primary System Pump duct v = 1.5 m/s M = 570 tons M = 855 tons M = 589 tons (8 SGs & 4 PPs) M = 3596 tons Total Mass of Lead = 5954 tons DHR v = 0.15 m/s M = 170 tons DHR M = 174 t Core v = 1 m/s

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, EFIT Primary Pump Characteristic

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, XT- ADS General Arrangement

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, XT- ADS General Arrangement

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, XT- ADS Primary Heat Exchanger

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, Core Mass Flow Rates Fuel A: 4518 kg/s By Pass: 296 kg/s Dummy A:1258 kg/s Target: 206 kg/s Storage F: 90 kg/s Others: 631 kg/s Core Pressure Drop Mass flow rate: 4518 kg/s Pressure drop: Pa Core v = 1.5 m/s Pump (N° 2) mfr/pump: 3500 kg/s ΔP pump : Pa Pump duct v = 1.9 m/s Δp pump = 0.5 ξ ρ v 2 ξ= 2.5 pump working ξ= 3.3 pump not locked ξ= 4.8 pump locked PHX (N° 4) mfr/PHX: 1750 kg/s ΔP PHX = Pa v = 1 m/s Mass Flow Rate, Pressure Drops and Free Levels In the XT-ADS Primary System Data for primary system design

EUROTRANS: WP1.5 Technical meeting, Bologna, May 28-29, XT- ADS Primary Pump Characteristic