Thermal-hydraulic phenomena

Подпись: performance of performance ofThermal-hydraulic phenomena and related parameter ranges that characterize the passive systems do not differ, in general, from phenomena that characterize the systems equipped with active components. This is specifically true for transient conditions occurring during safety relevant scenarios.

In other words, one can say that friction pressure drops or heat transfer coefficients are affected by local velocity and void fraction and not by the driving force that establishes those conditions, e. g. gravity head or centrifugal pump. The same can be repeated for more complex phenomena like two phase critical flow or counter-current flow limiting.

Thus, a large number of thermal-hydraulic phenomena that are expected to occur in passive systems during accident are classified in the OECD/NEA/CSNI documents ‘separate effect’ (SE) and ‘integral effect’ (IE) reported as references 19 and 20, hereafter. However, specific layout of passive systems and combination of parameter ranges brought the need of expanding the original list of phenomena in the same references 19 and 20. This was done in reference 21, where, mainly the passive systems proposed at the time of issuing of the report (1996) were considered.

The ‘expanded’ OECD/NEA list of phenomena for passive systems was up-graded in IAEA CRP on Natural Circulation Phenomena, Modeling and Reliability of Passive Safety Systems that Utilize Natural Circulation, considering the recently proposed passive systems by the industry. The description of the individual phenomena is given in the Appendix for the sake of completeness.

The identification and characterization of additional (i. e. with reference to the original SE and IE lists) phenomena for passive systems is presented in Table 1, which includes two main columns, other than the first column with numbering, which is consistent with the phenomena numbering in reference 19:

• Column 2: phenomena identification;

• Column 3: phenomena characterization based upon the individual phenomena description in the Appendix, considering the key layout of systems described in Sections 2 and 3.

The content of Table 1 is self-standing and directly understandable including the supporting description provided in the Appendix (as already mentioned). However, the following additional items should be noted:

• Specific geometry configurations or range of variations of affecting thermal-hydraulic parameters justify the presence of phenomena at rows 2, 5, 6 7 and 14 in both the present list and the list in reference 19. This is specifically true in the case of phenomenon 6 (natural circulation) that is expected to occur whenever a gravity environment exists.

• Natural circulation is also at the origin of the Core-make up Tank performance, phenomenon at row 15 in Table 1. However, the simultaneous presence of stratification in the tank, the possible condensation with level formation inside the tank, the specific loop connection and the values of boundary and initial conditions, suggest the consideration of a separate phenomenon.

TABLE 1. IDENTIFICATION AND CHARACTERIZATION OF PHENOMENA FOR PASSIVE SAFETY SYSTEMS

Phenomena identification

Characterizing thermal-hydraulic aspect

1

Behaviour in large pools of liquid

Thermal stratification

Natural/forced convection and circulation

Steam condensation (e. g. chugging, etc.)

Heat and mass transfer at the upper interface (e. g. vaporization)

Liquid draining from small openings (steam and gas transport)

2

Effects of non-condensable gases on condensation heat transfer

Effect on mixture to wall heat transfer coefficient

Mixing with liquid phase

Mixing with steam phase

Stratification in large volumes at very low velocities

3

Condensation on containment structures

Coupling with conduction in larger structures

4

Behaviour of containment emergency systems (PCCS, external air cooling, etc.)

Interaction with primary cooling loops

5

Thermo-fluid dynamics and pressure drops in various geometrical configurations

3-D large flow paths e. g. around open doors and stair wells, connection of big pipes with pools, etc.

Gas liquid phase separation at low Re and in laminar flow

Local pressure drops

6

Natural circulation

Interaction among parallel circulation loops inside and outside the vessel

Influence of non-condensable gases

Stability

Reflux condensation

7

Steam liquid interaction

Direct condensation

Pressure waves due to condensation

8

Gravity driven cooling and accumulator behaviour

Core cooling and core flooding

9

Liquid temperature stratification

Lower plenum of vessel

Down-comer of vessel

Horizontal/vertical piping

13

Behaviour of emergency heat exchangers and isolation condensers

Low pressure phenomena

14

Stratification and mixing of boron

Interaction between chemical and thermo-hydraulic problems

Time delay for the boron to become effective in the core

15

Core make-up tank behaviour

Thermal stratification

Natural Circulation

• The phenomenon at row 3 is a containment related phenomenon: the phenomena discussed in the (OECD/CSNI) report at reference 22 should be connected for completeness with the present one.

• The phenomenon at row 9 is also relevant for characterizing the phenomenon at row 1: geometry peculiarities and boundary conditions suggest keeping two separate phenomena in the present list.

• The accumulator behaviour is at the origin of an individual phenomenon considered in reference 17. Furthermore, the accumulator performance is driven by gas pressure. However, other than the ‘passive nature’ for the component behaviour, similarity in geometrical configuration and in the ranges of variations of relevant parameters suggested to consider ‘accumulator behaviour’ together with ‘gravity flooding’.

• The list of relevant thermal-hydraulic aspects in the 3rd column of the table can be expanded consistently with descriptions in Sections 2 and 3, and, also, in the Appendix: an effort to make fully comprehensive or exhaustive, the contents of the information in this column has not been attempted.