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VGB POWERTECH 7 (2021) - International Journal for Generation and Storage of Electricity and Heat

VGB PowerTech - International Journal for Generation and Storage of Electricity and Heat. Issue 7 (2021). Technical Journal of the VGB PowerTech Association. Energy is us! Optimisation of power plants. Thermal waste utilisation.

VGB PowerTech - International Journal for Generation and Storage of Electricity and Heat. Issue 7 (2021).
Technical Journal of the VGB PowerTech Association. Energy is us!
Optimisation of power plants. Thermal waste utilisation.

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<strong>VGB</strong> PowerTech 7 l <strong>2021</strong><br />

Study on the integrity <strong>of</strong> containment against hydrogen threats<br />

Review <strong>of</strong> PSA results<br />

Selection <strong>of</strong> initiating events among<br />

PSA results <strong>for</strong> severe accident analysis<br />

Severe accident analysis<br />

(using the MAAP5 code)<br />

3D analysis <strong>of</strong> hydrogen behavior <strong>and</strong><br />

combustion in the containment<br />

(using the GASFLOW-MPI code)<br />

3D analysis <strong>of</strong> structural response <strong>for</strong><br />

the integrity <strong>of</strong> containment<br />

(using the ABAQUS code)<br />

under severe accident conditions The<br />

Westinghouse-type 650 MWe PWR was<br />

used as the reference PWR <strong>for</strong> the evaluation.<br />

. A detailed assessment <strong>of</strong> the hydrogen<br />

threat in the containment was conducted<br />

using a 3D analysis. F i g u r e 1<br />

shows the assessment procedure in this<br />

study. In section 2, in order to review the<br />

integrity <strong>of</strong> the containment against hydrogen<br />

threats, accident scenarios were first<br />

chosen <strong>for</strong> the analysis <strong>of</strong> severe accidents.<br />

Subsequently, a severe accident analysis<br />

was per<strong>for</strong>med to determine the mass <strong>and</strong><br />

energy discharges to the containment during<br />

severe accidents. With the obtained<br />

mass <strong>and</strong> energy data, the static pressure<br />

in the containment was calculated in the<br />

event <strong>of</strong> hydrogen combustion in section 3.<br />

Then, the responses <strong>of</strong> the containment<br />

structure were evaluated on the basis <strong>of</strong><br />

the combustion static pressure <strong>of</strong> hydrogen.<br />

Finally, the integrity <strong>of</strong> the containment<br />

against hydrogen threats under severe<br />

accident conditions was evaluated in<br />

section 4 <strong>and</strong> conclusion.<br />

2. Selection <strong>of</strong> accident<br />

sequences <strong>and</strong> analysis<br />

Analysis <strong>for</strong><br />

in-containment<br />

against hydrogen<br />

threats<br />

Analysis <strong>for</strong> the structure <strong>of</strong><br />

containment against<br />

hydrogen threats<br />

Fig. 1. Overall procedure <strong>of</strong> the comprehensive analysis on the integrity <strong>of</strong> containment against<br />

hydrogen threats.<br />

Tab. 1. Level 1 PSA sequences <strong>of</strong> the reference<br />

plant.<br />

Sequences Percent [%]<br />

LOCCW 70.99<br />

LOOP 6.06<br />

MLOCA 2.08<br />

SLOCA 1.22<br />

Other transients 19.65<br />

Tab. 2. Key characteristics <strong>of</strong> the reference<br />

plant (WH-650MWe) [5].<br />

Parameter<br />

Value<br />

Reactor Power (MWth) 1,876<br />

Mass <strong>of</strong> zircaloy (lb) 25,240<br />

RCS operating pressure (psig) 2,235<br />

Hot leg/ Cold leg temperature ( o F) 616.6/549.4<br />

Containment design pressure (psig) 44.8<br />

Containment free volume (ft 3 ) 1.44x10 6<br />

Hydrogen control system<br />

PARs<br />

the atmosphere in the containment with<br />

the progress <strong>of</strong> the severe accident, were<br />

evaluated. Accident sequences were chosen<br />

based on the PDS (Plant Damage Status)<br />

[5]. In addition, the characteristics <strong>of</strong><br />

the accidents <strong>and</strong> the location where hydrogen<br />

is discharged to the containment<br />

were considered. As a result, the LOCCW<br />

(Loss Of Component Cooling Water) scenario,<br />

<strong>and</strong> LOOP (Loss Of Offsite Power)<br />

scenario were selected as the accident cases<br />

<strong>for</strong> the analyses, <strong>and</strong> the accidents with<br />

the same characteristics <strong>of</strong> transient accidents<br />

<strong>and</strong> discharge points were excluded.<br />

Additionally, the SLOCA (Small Break Loss<br />

Of Coolant Accident) <strong>and</strong> MLOCA (Medium<br />

break Loss Of Coolant Accident), which<br />

are ranked high in terms <strong>of</strong> the PDS, were<br />

selected. Ta b l e 1 shows the selected scenarios<br />

are dominant sequences in PSA results.<br />

The mass <strong>and</strong> energy discharge quantities<br />

<strong>for</strong> the selected accidents were calculated<br />

using the MAAP5 severe accident analysis<br />

code [7]. The MAAP5 is an integrated system<br />

analysis code used to evaluate severe<br />

accidents <strong>of</strong> NPPs. As a result <strong>of</strong> these analyses,<br />

the gas composition <strong>and</strong> thermal-hydraulic<br />

results, including the hydrogen<br />

concentration in the containment, were<br />

obtained. Only PARs were considered <strong>for</strong><br />

hydrogen control. The NUKEM correlation,<br />

which is the most conservative among<br />

the hydrogen removal rate correlations,<br />

was applied to calculate the PAR removal<br />

rate.<br />

The MAAP5 nodalization was composed <strong>of</strong><br />

the containment comprised 28 nodes,<br />

55 flow paths, <strong>and</strong> a total <strong>of</strong> 237 heat sinks,<br />

as shown in F i g u r e 2 . Key characteristics<br />

<strong>of</strong> the reference plant <strong>for</strong> severe accident<br />

analysis were shown in Ta b l e 2 . Ta -<br />

b l e 3 summarizes the results <strong>of</strong> the severe<br />

accident analysis obtained using the<br />

MAAP5, including the timing <strong>of</strong> the occurrence<br />

<strong>of</strong> major events such as core uncover,<br />

core melt progression, corium relocation<br />

into the lower head, <strong>and</strong> reactor vessel failure.<br />

In addition, it is possible to check the<br />

maximum average hydrogen concentration<br />

<strong>of</strong> the containment in each accident scenario.<br />

From the accident analysis results,<br />

the highest average hydrogen concentration,<br />

6.43 vol. %, is detected in the case <strong>of</strong><br />

MLOCA. This value confirms that hydrogen<br />

is sufficiently controlled below the<br />

regulatory st<strong>and</strong>ard, which stipulates that<br />

the hydrogen concentration must be managed<br />

at an average value <strong>of</strong> 10 vol. % or<br />

less. F i g u r e 3 . shows the typical steam<br />

Accident sequences were selected <strong>for</strong> the<br />

analysis <strong>of</strong> severe accidents. To choose the<br />

accident sequences, accident scenarios<br />

based on the results <strong>of</strong> a PSA (Probabilistic<br />

Safety Assessment) <strong>of</strong> the reference plant<br />

were referred. A 3D analysis <strong>of</strong> the containment<br />

under severe accident conditions was<br />

per<strong>for</strong>med to evaluate its structural integrity<br />

against hydrogen threat. First, the<br />

thermal-hydraulic conditions, such as the<br />

pressure, temperature, <strong>and</strong> composition <strong>of</strong><br />

Tab. 3. Severe accident progression <strong>and</strong> maximum hydrogen fraction in containment.<br />

Cases LOCCW LOOP MLOCA SLOCA<br />

Core Uncover [h] 3.5 2.25 0.04 4.77<br />

Max. Core Temperature<br />

exceeds 2500K [h]<br />

Corium relocation into Lower<br />

Head [h]<br />

6.74 3.37 7.69 5.67<br />

8.87 5.75 9.28 7.10<br />

Reactor Vessel Failure [h] 12.88 6.03 10.67 8.38<br />

Max. Hydrogen fraction [-] 0.05067 0.04522 0.06434 0.06333<br />

71

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