Cable in Conduit Conductor (CICC) quench modelling

Similar documents
RESIDENTIAL WATER DISTRIBUTION

MASSIVE GAS INJECTION SYSTEMS FOR DISRUPTION MITIGATION ON THE DIII-D TOKAMAK

MONROE BROTHERS LTD Customer Sigmaphi Project JLab Dipole Safety Relief MB / Description Chimney Vent Capacity & Pressure Drop 301 Issue 1

Internal Arc Simulation in MV/LV Substations. Charles BESNARD 8 11 June 2009

Transient Analyses In Relief Systems

ASSIGNMENT 2 CHE 3473

ASSIGNMENT 2 CHE 3473

Heat Pump Connections and Interior Piping

HTR Systems and Components

for Building facilities Industrial facilities etc.,multipurpose Pilot operated type(high capacity)

INTERNATIONAL JOURNAL OF ENGINEERING SCIENCES & RESEARCH TECHNOLOGY Dynamic Model of Pressure Regulating Valve Ahmed Abed *

Analysis of Pressure Rise During Internal Arc Faults in Switchgear

TECHNICAL BULLETIN CRYOGENIC APPLICATION SERVICES. website:

Risk Assessment for ITER TF Coil Manufacturing )

AIRFLOW GENERATION IN A TUNNEL USING A SACCARDO VENTILATION SYSTEM AGAINST THE BUOYANCY EFFECT PRODUCED BY A FIRE

PIG MOTION AND DYNAMICS IN COMPLEX GAS NETWORKS. Dr Aidan O Donoghue, Pipeline Research Limited, Glasgow

SUMMARY OF THE EXPERIMENTAL STUDIES OF COLD HELIUM PROPAGATION ALONG A SCALE MODEL OF THE LHC TUNNEL

The API states the following about tube rupture for a shell-and-tube heat exchangers:

1 SE/P-02. Experimental and Analytical Studies on Thermal-Hydraulic Performance of a Vacuum Vessel Pressure Suppression System in ITER

IMPROVED XENON LOADING EQUIPMENT WITH LOADING CAPACITY UP TO 1200 KG FOR ALPHABUS

AN EXPERIMENTAL INVESTIGATION ON HELIUM LIQUEFACTION USING TWO-STAGE GIFFORD McMAHON CRYOCOOLER

1.2 Example 1: A simple hydraulic system

Bubble Elimination Device in Hydraulic Systems

Gas Gathering System Modeling The Pipeline Pressure Loss Match

THERMO-HYDRAULIC ANALYSIS OF FORCED FLOW HELIUM COOLED CRYOPANELS OF CRYOPUMP USING VENECIA CODE

Inoxair. Repair Manual. Content. Edition: 12/2010. Subject to technical changes for reasons of the continous development.

PRELIMINARY PIPE STRESS ANALYSIS OF HIGH PRESSURE, HIGH TEMPERATURE EXPERIMENTAL HELIUM COOLING SYSTEM

SOLAR 93 THE 1993 AMERICAN SOLAR ENERGY SOCIETY ANNUAL CONFERENCE. Washington, DC April 22028,1993. Editors: S. M. Burley M. E.

The model of thermal response of Liquefied Petroleum Gas Tanks subjected to accidental heat input

SHUTDOWN SYSTEMS: SDS1 AND SDS2

Basic Hydraulics. Module 4: Flow Control Valves & Pressure Relief Valves. Academic Services PREPARED BY. January 2012

Steam generator tube rupture analysis using dynamic simulation

Gas Vapor Injection on Refrigerant Cycle Using Piston Technology

Loss of Vacuum Experiments on a Superfluid Helium Vessel

National Accelerator Laboratory

Fermilab MTF Cryogenic System & Vertical RF Cavity Test Facility. Yuenian Huang, on behalf of Fermilab, TD/TID May 11, 2006

A Study of Pressure Safety Valve Response Times under Transient Overpressures

C&G 2395 Exam Paper April Section A - All questions carry equal marks. Answer all three questions. Show all calculations.

Profile LFR-43 HELENA ITALY. Italian National Agency for New Technologies, Energy and Sustainable Economic Development, C.R. ENEA Brasimone, Italy

Hazard Operability Analysis

Experimental Verification of Integrated Pressure Suppression Systems in Fusion Reactors at In-Vessel Loss-of -Coolant Events

Enter your parameter set number (1-27)

Helium Management of the ESS Target and Monolith Systems

Free Surface Flow Simulation with ACUSIM in the Water Industry

Calculations of hydraulic resistance of simple pipelines for liquid viscous and non-newtonian products.

This portion of the piping tutorial covers control valve sizing, control valves, and the use of nodes.

CFD Flow Analysis of a Refrigerant inside Adiabatic Capillary Tube

4.1 Why is the Equilibrium Diameter Important?

Micro Channel Recuperator for a Reverse Brayton Cycle Cryocooler

Investigation on Divergent Exit Curvature Effect on Nozzle Pressure Ratio of Supersonic Convergent Divergent Nozzle

First Experimental Data of the Cryogenic Safety Test Facility PICARD

Installation Operation Maintenance

OPTIMIZATION OF SINGLE STAGE AXIAL FLOW COMPRESSOR FOR DIFFERENT ROTATIONAL SPEED USING CFD

MODELING&SIMULATION EXTRAPOLATED INTERNAL ARC TEST RESULTS: A COUPLED FLUID-STRUCTURAL TRANSIENT METHODOLOGY

NUMERICAL INVESTIGATION OF THE FLOW BEHAVIOUR IN A MODERN TRAFFIC TUNNEL IN CASE OF FIRE INCIDENT

AC : MEASUREMENT OF HYDROGEN IN HELIUM FLOW

ANALYSIS OF HEAT TRANSFER THROUGH EXTERNAL FINS USING CFD TOOL

Tutorial. BOSfluids. Relief valve

Control Valve : The Final Control Element. Nimish Shah

University of Cincinnati

Product Technical Bulletin #48

An Investigative and Synoptic Review on Helium Liquefaction Using a Commercial 4 K Gifford- McMahon Cryocooler

Single Phase Pressure Drop and Flow Distribution in Brazed Plate Heat Exchangers

Modelling of Pressurised Pipes within InfoWorks ICM and CS

Computational fluid dynamics analysis of a mixed flow pump impeller

Information Sheet. About this information sheet. Floor and wall loadings. Attachment of process module to floor. PlasmaPro Estrelas100

Test Plans & Test Results

EDEXCEL NATIONALS UNIT 6 MECHANICAL PRINCIPLES and APPLICATIONS. ASSIGNMENT No. 4

2/2-Way Solenoid Control Valve

ZIN Technologies PHi Engineering Support. PHi-RPT CFD Analysis of Large Bubble Mixing. June 26, 2006

JT Micro Compressor Test Results

FLUID POWER FLUID POWER EQUIPMENT TUTORIAL OTHER FLUID POWER VALVES. This work covers part of outcome 2 of the Edexcel standard module:

Tube rupture in a natural gas heater

Technical Specifications of Hydrogen Isotope Handling and Recovery System

Návrh vratného kanálu u dvoustupňového kompresoru Return channel design of the two stage compressor

International Journal of Technical Research and Applications e-issn: , Volume 4, Issue 3 (May-June, 2016), PP.

Pilot HON 625. Entwurf. Product information. serving the gas industry worldwide

2/2-Way Solenoid Control Valve

CONSIDERATION OF DENSITY VARIATIONS IN THE DESIGN OF A VENTILATION SYSTEM FOR ROAD TUNNELS

OIL AND GAS INDUSTRY

Effect of Inlet Clearance Gap on the Performance of an Industrial Centrifugal Blower with Parallel Wall Volute

A Brief Introduction to Helium Liquefaction At ITER

A Numerical Study of the Performance of a Heat Exchanger for a Miniature Joule-Thomson Refrigerator

23.1 Functions, Basic Configuration, and Interfaces

Introduction. Part one: Identify the Hydraulic Trainer Components

XCFD4NRS. Experiments and CFD Codes Application to Nuclear Reactor Safety. OECD/NEA & International Atomic Energy Agency (IAEA) Workshop

Earlier Lecture. In the earlier lecture, we have seen Kapitza & Heylandt systems which are the modifications of the Claude System.

Development of a Shock Loading Simulation Facility

Oxford Instruments Plasma Technology. PlasmaPro NGP80. Installation Data Sheet. Original Instructions.

Undertow - Zonation of Flow in Broken Wave Bores

Instruction Manual. Pipe Friction Training Panel

Magnet and RF Cavity Test Stand Design. Tom Peterson, SLAC USPAS January, 2017

Courses of Instruction: Controlling and Monitoring of Pipelines

CFD Simulation of the Flow Through Reciprocating Compressor Self-Acting Valves

Request Number IR1-12: Flow Passage. Information Request

High Performance BSP Dial Up Pattern Pressure Reducing Valve

Profile LFR-45 LIFUS5 ITALY. Italian National Agency for New Technologies, Energy and Sustainable Economic Development, C.R. ENEA Brasimone, Italy

LONGITUDINAL AIR VELOCITY CONTROL IN A ROAD TUNNEL DURING A FIRE EVENT

Fluid Flow. Link. Flow» P 1 P 2 Figure 1. Flow Model

VISIMIX LAMINAR. BLENDING OF NON-NEWTONIAN LIQUID. POWER. CIRCULATION. MIXING TIME.

Transcription:

DEMO SAMPLE Cable in Conduit Conductor (CICC) quench modelling

This demo gives an example of quench simulation for a Central Solenoid (CS). CS is divided into geometrically identical sections (see Fig. ) wounded by Cable-in-Conduit Conductor (CICC). Each section consists of CICC double pancakes. CS cooling is provided by supercritical helium (SHe) flow in parallel for all pancakes. Helium inlet is at the innermost turn of each pancake and outlet is at outermost turn. Quench occurs in CICC s of section CSL. Figure. CS sections with lower/upper buffer zones

It is assumed that CSL quench is initiated in each innermost turns of CSL pancakes at 79s of a regular plasma pulse, when constant and maximal currents (~ka) excite different CS sections. The VENECIA model of CS includes CS and an external cooling circuit. CS is modelled as CICC pancakes (C-:-C+C87-:-C7), inlet (C-:-C3) and outlet (C3-:-C8) tubes, supply (C733-:-C738) and return (C77-:-C73) feeders. The external cooling circuit is modelled as SHe heat exchangers (C7, C7), circulator (P), control valves (A, A), supply/return cryolines (C739, C7, C7, C73), relief valves (A3-:- A) with opening pressure of MPa and a set of quench line tubes (C7-:-C7) with the quench tank (V89). Control valve A is used to mitigate pulsed heat load from CS on the cryoplant. Control valve A provides protection of a SHe circulator when the pressure difference between the outlet and inlet of the circulator is close to the design limit on the pressure head. In each pancake, CICC is individually modelled with pares of SHe flows in the bundle and central channel which interact through mass- heat exchange. The CS model includes individual descriptions for magnetic field B, strains, AC losses and currents I distribution in each of CICC. These space/time descriptions for CS section CICC are provided through inputs as external data. Electrical field in CICC is calculated using a tabular description of superconductor properties parameterized via B, db/dr,, I and temperature T.

Figure. Hydraulic scheme of CS cooling cirquit. An inter turn and inter pancake heat exchange in CICC is modelled by solving a D thermal diffusion problem over CS cross-sections normal to the cable axis. Each cross-section includes 33 (x) stainless steel cable conduits, inter turn and inter pancake insulation, intersection insulation and upper/lower buffer zones. cross-sections taken for the simulation are meshed with 3. million nodes in total.

Figure 3. Meshing over a D CS cross-section. 7, nodes

Figure. Extraction from CS hydraulic model: CSL cooling circuit with position for cross sections # and #

Figure. Hydraulic scheme of quench lines Hydraulic parameters of CS cooling circuit and quench lines are listed in Table and Table. Channels # Cross section area, mm Hydraulic ID, mm Length, m Table. Parameters of CS cooling circuit Comments C-C..7 Cable space C87-C7 3. 9.7 Central pipe C-C3 78. Supply tubes C3-C8 78. Return tubes C77-C73 3 Return feeders C733-C738 3 Supply feeders C7,C73 3 8 39 Cryolines C7, C739 3 8 9 Cryolines C7, C7 3 SHEXs

Channels # Cross section area, mm Hydraulic ID, mm Length, m Table. Parameters of quench lines Comments C7 3 L3 lines С7 3 8 L3 lines C77 3 L3 lines C78 3 L3 lines C79 3 3 L3 lines C7 77 3 3 L3 lines C7 3 8 L3 lines C7 3 8 B lines С73 3 9 B lines C7 3 B lines C7 3 B lines C7 3 B lines C77 3 B lines C78 3 B lines C79 3 9 B lines C7 3 B lines C7 3 Blines C7 3 7 B lines С73 77 3 3 Line between L3 & B levels C7 9 3 Common line to quench tank C7 9 3 Common line to quench tank Volume V89 models a 8K quench tank of 7 m 3. This demo example is aimed to show VENECIA capabilities in modelling complex thermal hydraulic processes associated with CICC quench in CS, in particular - assessment of a minimum heat pulse energy for quench initiation; - simulation of normal zone evolution resulted in temperature (T) and helium pressure (P) rise caused by Joule heat deposited during quench; - investigation of protection strategy against overpressure in a cryogenic circuit via controlled opening of relief valves and evaluation of instant parameters of helium flows released from the CS; - prediction of temperature & pressure rise along quench lines. Simulation of CSL conductors quench allows revealing the conditions for helium release from CS through the relief valves and the maximum helium parameters along the quench lines. The demo simulation is only illustrative and has certain limitations due to taken for consideration the simplified quench scenario. Simulated CS behaviour is reduced to a s quench at constant currents in CS sections that corresponds to overheat conditions without quench protection and fast energy discharge. Modelling of complex phenomena occurred in a cryomagnetic system in case of quench and CICC protection against overheating requires more detailed description beyond demo purposes and is a subject of contractual investigations.

Initial conditions for modelling The quench is initiated by a uniform heat pulse applied to innermost turns of CSL CICC s when the other CICCs of CS have zero currents. A W/m heat pulse with a.s duration is applied at the end of plasma pulse (79s) when a s plateau of constant maximum currents in sections (~ ka) is supported. The magnetic field in the fired innermost turns is close to the maximal value of T. As initial thermal-hydraulic conditions for CS quench simulation, pre-determined data are used from input files CS3.BS and HEATD_.BAS that gathered in a CS simulation at normal operation. For illustration, the plots below shows CS behaviour at normal operation for a 8s regular plasma pulse..8. Temperature, K...8... 8 8 x, m Figure. Variation of CICC temperature in middle double pancakes of six CS sections CS3L, CSL, CSL, CSU, CSU, CS3U during a 8 s plasma pulse. Normal operation

Temperature, K.. 8.7 7.8 (8) s 8 3 8 8 38 8 8 8 89 9 39. x, m Figure 7. Temperature variation along pancake # (middle of CSL). Normal operation The full set of inputs for the demo quench simulation is available in the input files DEMO.IN and HEATD_.IN. Files VENECIA.MAT and ETABD_.IN describe thermal properties of different materials in the CS assembly and electrical properties of CICC, correspondingly.

Basic simulated results for CS quench started in CSL section Temperatura, K 3 3. s.. 3 3... 7 8 9 N N3 x, m Temperature evolution of CICC bundle for adjacent pancakes # and # of quenched CS section CSL

Temperatura, K 3 3. s.. 3 3... 7 8 9 N N3 x, m Helium temperature evolution in central channel for adjacent pancakes # and # of quenched CS section CSL

Pressure, MPa 8. s.. 3 3... 7 8 9 N N3 8 x, m Helium pressure in cable space for adjacent pancakes # and # of quenched CS section CSL

Velocity, m/s N. s.. 3 3... 7 8 9 N x, m Helium velocity in cable space for adjacent pancakes # and # of quenched CS section CSL

3 N N Mass flow rate, g/s 3 x, m. s.. 3 3... 7 8 9 Helium mass flow rate in cable space for adjacent pancakes # and # of quenched CS section CSL

N N Mass flow rate, g/s x, m. s.. 3 3... 7 8 9 Helium mass flow rate in central channel for adjacent pancakes # and # of quenched CS section CSL

Temperature map for cross section # of CS model in vicinity of adjacent sections CS3L and CSL at t=.s

Temperature map for cross section # of CS model in vicinity of adjacent sections CS3L and CSL at t=.s

Temperature map for cross section # of model in vicinity of adjacent CS sections CS3L and CSL at t=.s (zoom-in of marked region from previous plot)

Temperature, K 3 3. s.. 3 3... 7 8 9 3 9 38 x, m Helium temperature variation in inlet feeders (C733, C73, C73, C73, C737, C738, each 3 m in length) for six CS sections: CS3L, CSL, CSL, CSU, CSU, CS3U

Pressure, MPa 7 3. s.. 3 3... 7 8 9 3 9 38 x, m Helium pressure variation in inlet feeders for six CS sections

Velocity, m/s 3 3. s.. 3 3... 7 8 9 3 9 38 x, m Helium velocity variation in inlet feeders for six CS sections

dm/dt, kg/s. s.. 3 3... 7 8 9 3 9 38 x, m Helium mass flow rate variation in inlet feeders for six CS sections

3 N # & # N 9 8 B, T 7 3 x, m Local distribution of magnetic field B along CICC in pancakes # & #

.73.7.7.7 Strain.77.78.79.8 # & #.8 x, m Local distribution of strain along CICC in pancakes # & #

ExI, W/m N N. s.. 3 3... 7 8 9.8... 8 x, m Variation of Joule heat along CICC in pancakes # & # at constant current of ka. NOTE: Plateau of Joule heat at a level ~8kW/m is explained by limited input data on CICC property in file ETABD_.IN, where the tabulated maximal temperature is given as 3K, so for T>3K electric field E(T, B, db/dr,, I)= E(3K, B, db/dr,, I).

.. A A A8 dm/dt, kg/s.8... 3 7 8 9 t, s Helium mass flow rate at inlets of relief valves A, A, A8 7 A3 A A7 dm/dt, kg/s 3 3 7 8 9 t, s Helium mass flow rate at inlets of relief valves A3, A, A7

.3.3 A A A. dm/dt, kg/s.... 3 7 8 9 t, s Helium mass flow rate at inlets of relief valves A, A, A 7 A A A8 Opening, mm^ 3 3 7 8 9 t, s Variation of opening for relief valves A, A, A8

. P_open.8. Pressure, MPa...8. V9 (A3,A,A7) V (A9,A,A3). V (A,A,A8) V (A,A,A). 3 7 8 9 t, s Helium pressure at inlets of the safety relief valves 3 3 V9 (A3,A,A7) V (A9,A,A3) V (A,A,A8) V (A,A,A) Temperature, K 3 7 8 9 t, s Helium temperature at inlets of the safety relief valves

.. P T. Pressure, MPa.3 98 Temperature, K. 9. 8. 8 3 7 8 9 t, s Evolution of helium pressure and temperature inside quench tank V89 due to helium release via safety valves

3 C7-C7, 73, 7, 7 3 T, K. s.. 3 3... 7 8 9 x, m Evolution of temperature along selected portion of quench lines (see total layout of quench lines in Fig. )

P, MPa.....3.3. C7-C7, 73, 7, 7. s.. 3 3... 7 8 9.... x, m Evolution of pressure along selected portion of quench lines (see total layout of quench lines in Fig. )

3. P 3. dm/dt, kg/s.. 8 t, s Flow rate variation of circulator P in accordance with its characteristic m - P.9 P.8.7 DP, MPa....3 3 7 8 9 t, s Pressure head variation in circulator P limited by control valve A opening

A Opening, mm^ 3 3 7 8 9 t, s Variation of control valve A opening A dm/dt, kg/s 3 7 8 9 t, s Variation of control valve A mass flow rate