pre-test analysis of molten salt natural circulation loop using flinak...

5
210 Special Issue | October 2014 BARC NEWSLETTER Founder’s Day PRE-TEST ANALYSIS OF MOLTEN SALT NATURAL CIRCULATION LOOP USING FLiNaK SALT A.K. Srivastava, A. Borgohain, N.K. Maheshwari and P.K. Vijayan Reactor Engineering Division Abstract Molten Salt Natural Circulation Loop (MSNCL) has been setup in BARC. It is a rectangular loop comprising of five components- heater, cooler, melt tank, expansion tank and loop piping. A steady state and transient analysis for the MSNCL has been performed using a one dimensional finite difference code, LBENC. Molten fluoride salt, eutectic mixture of lithium, sodium and potassium fluoride (FLiNaK) has been used as heat transfer medium for the analysis. Various transients such as startup of natural circulation, loss of heat sink, heater trip and step power increase have been analyzed for different orientation of heater and cooler. This Paper received the Best Poster Presentation Award at the [International Conference on Molten Salts In Nuclear Technology] held at Mumbai, from Jan. 9-11, 2013 Introduction Present water cooled nuclear reactors have a limitation of temperature not going beyond 325 o C. Increasing the system temperature increases the plant efficiency. Going beyond a certain temperature in case of water, need its pressurization which causes safety concern. Keeping in mind the cost and safety issues, researchers have a challenge to develop coolants for nuclear reactors which can be operated at higher temperature and low pressure. Molten fluoride salt mixtures have been considered as heat transfer media for core heat removal in advanced nuclear reactors as they have high boiling points. This allows reactors to be operated at high temperature and nearly atmospheric pressure. The high temperature heat is proposed to be used for generating hydrogen by thermo-chemical splitting of water. Studies of natural circulation with water are abundant in literature. Both experimental and theoretical studies on the nature of unstable flow were performed by Vijayan et. al. [1]. There are some numerical studies for stability and other transient analysis of single- phase natural circulation loops [2-5]. Furthermore, the RELAP5, CATHARE2, and ATHLET system codes have been used in transient analysis for single-phase natural circulation loops [6-8]. The study of natural circulation in molten salt is still quite limited. Although a few analytical works exist for the thermal-hydraulics of molten salt cooled reactors [9], little experimental data have been published to demonstrate the thermal-hydraulic performance of molten salt-cooled systems. The paper deals with the analysis performed for steady state and transient behavior of MSNCL, installed in BARC using FLiNaK salt mixture. Natural Circulation Loop Detail Molten salt loop is a 15NB uniform diameter rectangular natural circulation loop as shown in Fig. 1(a) and Fig. 1(b). It comprises basically four components- heater, cooler, melt tank and expansion tank. The height and Home NEXT PREVIOUS ê ê CONTENTS

Upload: truongliem

Post on 17-Aug-2018

215 views

Category:

Documents


0 download

TRANSCRIPT

Page 1: PRE-TEST ANALYSIS OF MOLTEN SALT NATURAL CIRCULATION LOOP USING FLiNaK SALTbarc.gov.in/publications/nl/2014/spl2014/pdf/paper49.pdf · 210 Special Issue | October 2014 BARC NEWSLETTER

210 Special Issue | October 2014

BARC NEWSLETTERFounder’s DayPRE-TEST ANALYSIS OF MOLTEN SALT NATURAL

CIRCULATION LOOP USING FLiNaK SALT

A.K. Srivastava, A. Borgohain, N.K. Maheshwari and P.K. VijayanReactor Engineering Division

Abstract

Molten Salt Natural Circulation Loop (MSNCL) has been setup in BARC. It is a rectangular loop comprising of

five components- heater, cooler, melt tank, expansion tank and loop piping. A steady state and transient analysis

for the MSNCL has been performed using a one dimensional finite difference code, LBENC. Molten fluoride salt,

eutectic mixture of lithium, sodium and potassium fluoride (FLiNaK) has been used as heat transfer medium for

the analysis. Various transients such as startup of natural circulation, loss of heat sink, heater trip and step power

increase have been analyzed for different orientation of heater and cooler.

This Paper received the Best Poster Presentation Award at the [International Conference on Molten Salts In Nuclear Technology] held at Mumbai, from Jan. 9-11, 2013

Introduction

Present water cooled nuclear reactors have a limitation

of temperature not going beyond 325oC. Increasing

the system temperature increases the plant efficiency.

Going beyond a certain temperature in case of water,

need its pressurization which causes safety concern.

Keeping in mind the cost and safety issues, researchers

have a challenge to develop coolants for nuclear

reactors which can be operated at higher temperature

and low pressure. Molten fluoride salt mixtures have

been considered as heat transfer media for core heat

removal in advanced nuclear reactors as they have high

boiling points. This allows reactors to be operated at

high temperature and nearly atmospheric pressure.

The high temperature heat is proposed to be used for

generating hydrogen by thermo-chemical splitting of

water.

Studies of natural circulation with water are abundant

in literature. Both experimental and theoretical studies

on the nature of unstable flow were performed by

Vijayan et. al. [1]. There are some numerical studies

for stability and other transient analysis of single-

phase natural circulation loops [2-5]. Furthermore, the

RELAP5, CATHARE2, and ATHLET system codes have

been used in transient analysis for single-phase natural

circulation loops [6-8].

The study of natural circulation in molten salt is still

quite limited. Although a few analytical works exist for

the thermal-hydraulics of molten salt cooled reactors

[9], little experimental data have been published to

demonstrate the thermal-hydraulic performance of

molten salt-cooled systems.

The paper deals with the analysis performed for steady

state and transient behavior of MSNCL, installed in

BARC using FLiNaK salt mixture.

Natural Circulation Loop Detail

Molten salt loop is a 15NB uniform diameter rectangular

natural circulation loop as shown in Fig. 1(a) and Fig.

1(b). It comprises basically four components- heater,

cooler, melt tank and expansion tank. The height and

Home

NEXTPREVIOUS ê ê

CONTENTS

Page 2: PRE-TEST ANALYSIS OF MOLTEN SALT NATURAL CIRCULATION LOOP USING FLiNaK SALTbarc.gov.in/publications/nl/2014/spl2014/pdf/paper49.pdf · 210 Special Issue | October 2014 BARC NEWSLETTER

Special Issue | October 2014 211

BARC NEWSLETTERFounder’s Day

total length of the loop are 2000 mm and 6800 mm

respectively. The loop is designed in such a way that

the orientation of heater and cooler can be changed

to study its effect on natural circulation flow rate. Air

is used as secondary side coolant.

Analysis for Molten Salt Natural Circulation Loop (MSNCL)

This analysis has been performed using one

dimensional finite difference code LBENC [10]. The

code is validated with water and liquid metal [11]. This

study is performed for FLiNaK salt (eutectic mixture

of LiF-NaF-KF), proposed as a candidate coolant for

HTRs. For the sake of analysis, the loop geometries are

divided into segments. Each segment is then divided

into nodes. The number of nodes was taken as 20

for each segment of the loop. Pressure drop due to

sudden expansion, contraction, bends etc. associated

with each segment was accounted using suitable loss

co-efficient. Temperature dependent thermo-physical

properties [12] are considered for the analysis. The

transients performed with the help of LBENC code

include the loss of heat sink, heater trip and start-

up of natural circulation. Analysis is performed for

all four different orientations of heater and cooler

i.e. Horizontal Heater & Horizontal Cooler (HHHC),

Horizontal Heater & Vertical Cooler (HHVC), Vertical

Heater & Horizontal Cooler (VHHC) and Vertical

Heater and Vertical Cooler (VHVC). Prior to each

transient analysis, steady-state conditions are usually

established in the loop, which are the initial conditions

of the subsequent transient analyses.

Steady state mass flow rate

Steady state mass flow rate is calculated for different

heater power. Initially the fluid is in stagnant

condition, heater power is zero and temperature

of salt and the loop is 5000C. Heater power is then

increased to 1000W in steps of 200W. Fig. 2 shows

the calculated steady state mass flow rate at different

power for all the four orientations. On applying the

power at every step, the mass flow rate gives a steady

Fig. 1(a): Schematic of Molten Salt Natural Circulation Loop (MSNCL)

Fig. 1(b). Photograph of Molten Salt Natural Circulation Loop (MSNCL)

Page 3: PRE-TEST ANALYSIS OF MOLTEN SALT NATURAL CIRCULATION LOOP USING FLiNaK SALTbarc.gov.in/publications/nl/2014/spl2014/pdf/paper49.pdf · 210 Special Issue | October 2014 BARC NEWSLETTER

212 Special Issue | October 2014

BARC NEWSLETTERFounder’s Daystate value. The power step is allowed to change

after every 10000s. It is observed that the predicted

steady state flow rate is highest in HHHC orientation

and lowest in VHVC orientation at each power step.

This is because the effective elevation difference

between the hot and the cold leg, which is the

driving force for natural circulation, is highest (2000

mm) in HHHC orientation and lowest (500 mm) in

VHVC orientation. The effective elevation difference

for HHVC and VHHC orientations are 1300 mm and

1200 mm respectively.

Loss of Heat Sink

This analysis is carried out at 1000W power. Initially the

system is allowed to come in steady state at 1000W

heater power and then secondary side heat transfer

coefficient is set to 5W/(m2-K) at 10000s, a non-zero

small value to account heat loss from cooler. Fig. 4(a)

shows the transient mass flow rate variation for loss

of heat sink case for all the four orientations. Due to

unavailability of the cooler, the average temperature of

the molten salt starts increasing. It can be seen from

Fig. 4(a), after 10000s the mass flow rate suddenly

decreases. This decrement in mass flow rate continues

Fig. 2: Steady state mass flow rate vs. power in MSNCL

Start-up of natural circulation

Initially the fluid is in stagnant condition, heater

power is zero and temperature of salt and the loop

is 500 0C. Full power of 1000W is then applied to

the heater in a single step at 0s. Fig. 3(a) shows

the mass flow rate transient in start-up condition

for all the four orientations. As the salt gets heated

up, the mass flow rate starts increasing in the loop.

At initial stage, the salt flow rate is low due to its

inertia. Sudden application of full power causes a

peak in mass flow rate which comes almost to steady

state after 10000s. It can also be seen from Fig. 3(b)

that after 10000s the temperature at inlet/outlet of

heater and cooler reaches a constant value for VHHC

orientation.

Fig. 3(a): Variation of mass flow rate during start-up of natural circulation from stagnant condition

Fig. 3(b): Heater and Cooler Inlet/Outlet Temperature Variation for VHHC orientation

Page 4: PRE-TEST ANALYSIS OF MOLTEN SALT NATURAL CIRCULATION LOOP USING FLiNaK SALTbarc.gov.in/publications/nl/2014/spl2014/pdf/paper49.pdf · 210 Special Issue | October 2014 BARC NEWSLETTER

Special Issue | October 2014 213

BARC NEWSLETTERFounder’s Dayand goes towards zero as expected. This is because after

loss of heat sink the temperature difference between

hot leg and cold leg decreases and hence the diving

force. Figure 4(b), temperature transient, shows the

sudden temperature rise in the molten salt after loss

of heat sink for VHHC orientation. After t=10000s,

the temperature difference between the heater and

cooler decreases. The temperature of the loop suddenly

increases and reaches to 1000oC in just 2000s.

achieved at heater power of 1000W, then for the

transient heater power was set to zero in single

step at 10000s. Figure 6(a) and Fig. 6(b) show mass

flow rate and temperature transients respectively

following heater trip. Due to unavailability of the

heater, molten salt temperature starts decreasing

drastically. Mass flow rate also decreases continuously

because of reduction in the available driving head

i.e., temperature difference in hot leg and cold

leg. The transient is stopped as soon as molten salt

temperature reaches 454oC, the freezing point of the

FLiNaK salt mixture.

Fig. 4(a): Variation of mass flow rate during simulated loss of heat sink

Fig. 4(b): Heater and Cooler Inlet/Outlet Temperature Variation in VHHC orientation for simulated loss of heat sink

Heater Trip

This transient is realized by removing the applied

power from the heater. Initially a steady state was

Fig. 5(a): Variation of mass flow rate during the simulated loss of heater trip

Fig. 5(b): Heater and Cooler Inlet/Outlet Temperature Variation in VHHC orientation for simulated heater trip

Page 5: PRE-TEST ANALYSIS OF MOLTEN SALT NATURAL CIRCULATION LOOP USING FLiNaK SALTbarc.gov.in/publications/nl/2014/spl2014/pdf/paper49.pdf · 210 Special Issue | October 2014 BARC NEWSLETTER

214 Special Issue | October 2014

BARC NEWSLETTERFounder’s DayConclusions

A Pre-test analysis of MSNCL has been performed

using LBENC code. Various transients such as: startup

of natural circulation, loss of heat sink and heater trip

has been analyzed. Steady state mass flow rate has

been predicted for different heater power. Effect of

orientation of heater and cooler on all the transients

has been studied with the above analysis. The

experimental results are awaited for the comparison

of these results.

References

1. Vijayan, P.K, et al., 2004, 17th National and 6th

International ISHMT-ASME HMTC, 600-606.

2. Ambrosini, W., and Ferreri, J.C., 1998, NED, 183,

53–76.

3. Ambrosini, W. and Ferreri, J.C., 2003, Annals of

Nuclear Energy 30, 1505–1537.

4. Doster, J.M., Kendall, P.K., 1999, Nuclear Science

and Engineering, 132, 105–117

5. Cammarata, L., et al., 2003, Applied Thermal

Engineering 23, 965–977.

6. Vijayan, P.K., et al., 1995, NED 155, 623–641

7. Misale M., et al., 1999, Eurotherm Seminar, 6–8

September, Genoa, Italy.

8. Petruzzi, A., et al., 2001, CAMP Meeting, 23–25

April, Prague, Czech Republic.

9. Zhang et al., 2009, NED, 239 2778–2785

10. Jaiswal, B.K., et al., 2008, 19th National and 8th

International ISHMT-ASME HMTC, NHT-5/41B.

11. Jaiswal, B.K., Srivastava, A.K., Borgohain, A.,

Maheshwari, N.K., Vijayan, P.K., ICONE-19, May

16-19, 2011, Makuhari, Chiba, Japan

12. Y.M.Ferng, Kun-Yueh Lin, Chen-Wei Chi, Applied

Thermal Engineering 37 (2012) 235-240.