ermsar-07 –fzk-12-14 june07- karlsruhe revaporisation issues: an overview d. bottomley 1,.r.s....

ERMSAR-07 –FZK-12-14 June07- Karlsruhe

Revaporisation issues: an OverviewRevaporisation issues: an Overview

D. BottomleyD. Bottomley11, .R.S. Dickson, .R.S. Dickson22, T. Routamo, T. Routamo33, J. Dienstbier, J. Dienstbier44, A. Auvinen, A. Auvinen55, & N. Girault, & N. Girault66

11 JRC-ITU Karlsruhe (DE) JRC-ITU Karlsruhe (DE)2 2 Chalk River Laboratories, AECL (Canada)Chalk River Laboratories, AECL (Canada)33 Fortum Nuclear Services Ltd. (FIN) Fortum Nuclear Services Ltd. (FIN)4 4 UJV Rez (CZ)UJV Rez (CZ)5 5 VTT Espoo (FIN)VTT Espoo (FIN)6 6 IRSN Cadarache (FR)IRSN Cadarache (FR)

Presented by D..Bottomley - ITUPresented by D..Bottomley - ITU


• Introduction- current status • Experiments on Revaporisation –single effects & Phebus (VTT, ITU &

IRSN)• Modelling of revaporisation – SET’s, Integral tests (UJV & Fortum) • Use in severe accident analysis• Advances & future outlook

Outline of Talk


Revaporisation –a simple illustration

CsOH (g) or (CsOH)2 (g)

CsOH (ads)

1) Diffusion in oxide layer along grain boundaries and cracks during

deposition

Metal substrateCracks, defects in oxide

Outer Oxide

2) Diffusion out of oxide layer and cracks during revaporisation

along with direct desorption

Gas flow with changing T, Cp, composition, flow rate

CsOH (gb)

CsOH (ads) CsOH (ads) Chemical reactions with other compounds in the

deposit possible


Revaporisation: current status

• Fission products can rapidly deposit upon cooler surfaces but under various changes in

conditions can cause the deposited fission products (eg. Cs & I) volatilise again • Revaporisation was initially anticipated from decay heat reheating of deposits, but

changes in T, flow rate, or gas composition (with changes in Cp or pO2) are also causes. • Revaporisation was recognised as a source term factor in the late phase and an

especially dominant risk with the occurrence of a by-pass (eg. late stage steam generator rupture) . The Phebus REVAP project (FP5 Programme) had demonstrated the phenomenon for simple Cs deposits & for more complex deposits in steam and showed that it could be triggered with simple temperature or atmosphere variation. Also SETs from AEAT showed original deposition conditions greatly affected the extent of, & susceptibility to revaporisation.

• Understanding the revaporisation mechanisms both experimentally & from a modelling standpoint was important.


Phebus FPT1 : Revaporisation of vertical line deposits

Fig. a Revaporisation device with lead-shielded oven, diluter & filter with -detector above glove-box

Fig. b Diagram showing gas flow of Revaporisation device at ITU


Phebus - Revaporisation testing of deposits from FPT1 vertical line & FPT4 shroud

0.0

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stainless steel insteam (FPT1) porous ThO2 in N2 +8% H2 (FPT4)porous ThO2 in steam(FPT4)temperature FPT1

temperature FPT4

Revaporisation of fission product deposits (loss of Cs-137 activity at 661keV) upto 1000°C from different substrates of FPT1 (stainless steel vertical line) and FPT4 porous ThO2 shroud.Revaporisation from steel surfaces is rapid above 550C, it is slower and at higher temperatures from porous ceramic


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137Cs Station 3 (661.66 keV, 30 a)

Experimental phases

137Cs Station 2

Synthetic signal

Core Power [a.u.]

H2 production [a.u.]

Power level, hot leg Cs-137 activities and H2 production during FPT2 test.

Phébus FPT2 test profile: Revaporisation noted during the results evaluation

Note the final decrease in hot leg activity after reactor shutdown


Schematic Diagram of AECL HCE Facility

Ar/

2%H

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argo

n

air

gas-monitoring -spectrometer

direct-viewing -spectrometer

water supply pump

sample

furnace

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emergencysuction system

deposition tube

off-gasscrubber

1: flow meters and valves2: steam generator3: inlet oxygen sensor4: aerosol collector5: outlet oxygen sensor6: condenser

pyrometer

HCE3 Hot Cell apparatus used for the revaporisation testing of the deposits derived from sheathed CANDU fuel segments


AECL Revaporisation testing

•Vaporisation & Deposition •six characteristic CANDU materials used: Zircaloy 4, Zr-2.5Nb, stainless steel Types 403 and 410, Inconel-600 and carbon steel, were exposed to an air, steam, or steam + Ar stream in a ss thermal gradient tube downstream of the fuel sample at 160 - 600°C. XPS Spectroscopy showed Sn, Cs and Mo, with lesser amounts of Rb, Te and U in all coupon deposits. •Revaporisation•Coupon was heated to 700°C for 1800 s in a slow gas stream

•Air-deposited coupons were revaporised in air. •steam or steam + argon-deposited coupons were revaporized in Ar-2% H2.

•Post test counting (after 80 days to reduce background levels) detected 134Cs, 137Cs and 129mTe, with 103Ru and 106Ru in air & steam tests, and 110mAg detected in all three gas flows. Changes in isotope levels were consistent for an element.

•This indicates that the Cs & Ru revaporisation occurs in oxidising environments & Ag revaporisation in all atmospheres.


VTT forthcoming revaporisation testing facility

Objective: to determine fission product compounds formed by reactions on primary circuit piping surfaces.

• The sampling system will be identical to that of CHIP facility - facilitating comparison of the results• Sampling is designed to avoid losses due to 1) aerosol deposition or 2) vapour condensation as the sample cools from 1000°C to 150°C. • Size distribution and concentration of aerosol particles as well as chemical speciation of gaseous species are measured on-line.•Compounds transported as aerosol particles at high and at low temperature can be differentiated from the vapour phase and gaseous species•During 2007 the experimental facilities will be constructed and tested. •Gaseous iodine in the sampling lines and in the filters will be studied by radiotracers in 1st five experiments with the release of iodine by revaporisation of CsI sample in the 6th (final) test of 2007.•Samples containing compounds of boron, molybdenum, tellurium and uranium will be examined in the following years (2008/10).


Modelling of VTT single effect tests by UJV Réz (ASTEC v1.3)

a) VTT REVAP test 7 Calculated sample mass b) VTT REVAP test 7 Measured pulse rate

Experimental MethodCsOH solution or CsI powder labelled with 134Cs or 137Cs were put on type 304 stainless steel tray inside a furnace tube, dried in N2 flow at lower temperatures, then vaporized in steam flow. The temperature was gradually increased to 800C for CsI and to 1000C for CsOH.Gamma scanning was performed along the experimental tube and in time.

Comparison of model with test


Modelling of VTT single effect tests: UJV Réz (ASTEC v1.3)

ResultsCsIA relatively good agreement between the test and the calculation was found for all tests with CsI, see test 7 CsOHVaporisation is slightly slower in the final phase of the test, after temperature rise beyond 700C. However the CsOH modelling tended to be too fast in this final phase. Values found for CsOH partial vapour pressure varied by 100x – a probable source of inaccuracy for the modellers


Fortum engineering & VTT – Severe Accident Modelling (APROS SA)

h

S exp1dQ

SDSh

TR

MQpJ

The circuit of the PHEBUS FP facility in FPT1 was calculated.

The revaporisation model is based on the work by VTT and the revaporating

mass flux J [kg/s] is calculated from:

where:pS = saturation vapour pressure [Pa]M = molar mass of vapour[kg/mol]Q = volumetric flow rate of gas [m3/s]T = temperature [K]R= gas constant =8.3143 [J K-1 mol-1]D = binary diffusion coefficient [m2/s]S = area of revaporisation surface[m2]dh= hydraulic diameter of tube [m]Sh= Sherwood number.

Size classSmall(0.25 µm)

Medium (0.84 µm)

Large (3.4 µm)

Iodine 37 % 39 % 24 %

Caesium 6 % 21 % 73 %

Tellurium 44 % 37 % 19 %

The following input size distribution (as mass fractions) was used for the modeled FP groups for

modelling of FPT1.


APROS SA Modelling of Phebus FPT1

Vertical steam generator U-tube diagram and nodalisation.

(Hot leg has 3 nodes and the cold leg has 2 nodes)


Distribution of iodine, caesium and tellurium in FPT1 and in APROS SA calculations + revaporisation + sedimentation options

Iodine

0102030405060708090

100

Hot leg SG Cold leg OUT

% o

f T

ota

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ass

ExpABCD

Caesium

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100


% o

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ExpABCD

Tellurium

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% o

f T

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ExpABCD

Calculation case A B C D

Revaporisation Yes No Yes No

Sedimentation Yes Yes No No

All: deposited material was totally removed from the hot leg surfaces when the revaporisation model was turned on (A & C)

– close to exptl. resultsCs: when no revaporisation model, sedimentation active or not makes a significant difference (B & D). Cold leg deposits also

over-estimated

(OUT is the fraction passing through the system)


1) The REVAP circle have shown revaporisation can have a considerable source term impact as frequently these surface deposits are in equilibrium with the vapour. Thus changes in temperature, flow rate or atmosphere can result in a rapid revaporisation of Cs.

Experimental2) CsOH and Phebus FPT1 deposits (VTT & ITU testing) show Cs revaporises in steam atmospheres

similarly to CsOH & explains the caesium mobility observed in the Phébus FPT1.3) Cs revaporisation was also observed by IRSN after the FPT2 shutdown (it is a late phase risk).4) Revaporisation can occur under different atmospheres and substrates. Cs oxide/hydroxide deposits

on steel can revaporise under reducing, steam and inert atmospheres. Ceramic substrates show a slower and reduced release - probably with slower diffusion up through the pores.

5) AECL & FPT4 data also show that other major fission products such as Ru, Te or Mo revaporise as does Cs under various atmospheres.

Modelling6) Modelling by UJV has been able to reproduce the results for CsOH (single & mixed) deposits so

that the Cs model appears to be correct. However some of the Cs vapour pressure data may not be very accurate. Cs2MoO4 could also be a potential transport species.

9) The inclusion of revaporisation model by FORTUM in a full severe accident (SA) code has confirmed the Phebus FPT1 results. Cs fractional release beyond the steam generator is increased with all deposits in the hot leg (& upstream) being revaporised.

Conclusions


• More complex scenarios will be difficult to resolve within this programme.

• Both integral & single effect testing will still be necessary.

• Particularly interactions with resuspension, thermophoresis & diffusiophoresis mechanisms (especially with heavy deposits) need to be understood to properly estimate the source term impact.

Outlook

ermsar-07 –fzk-12-14 june07- karlsruhe revaporisation issues: an overview d. bottomley 1,.r.s....

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