Operational Reactor Safety

22.091 /22.903

Professor Andrew C. Kadak Professor of the Practice

Spring 2008

Lecture 2 3 :

Current Regulatory Issues

Present Situation

It doesn’t get any better than this for nuclear energy!

Very Good Nuc lear Regulatory Commission

Combined Construction Permit and Operating License

Early site permits supported by DOE

Concern about Global Climate Change

Ris i ng and highly volatile natural gas and oil prices

Great rhetoric from the Pres ident and Congress about need for nuc lear energy for env ironment, security and stability

Strong Pro-nuclear congressional l egislation in the Energy Policy Act of 2005.

Congress

P assed Energy Policy Act of 2005

N uclear energy provisions

P roduction tax credit - $ 200/kw for first movers

Loan guarantees

Insurance protection of up to $ 500 million for regulatory delays for first 2 plants.

E ffort to stimulate orders for new plants

D epartment of Energy working to develop advanced reactor designs as part of Generation IV reactors - 2030

Present New Market Offerings

AP-1000 (Westinghouse)

1 ,000 Mwe P WR

E SBWR (General Electric)

1390 Mwe - B WR

E PR ( Framatome A NP)

1 ,600 Mwe P WR

APWR ( Mitsubisi)_

1 ,700 Mwe PWR

Certified Designs

AP-600 (Westinghouse)

A BWR 1250 Mwe (General Electric)

System 80 + - 1 300 Mwe ( Westinghouse/CE)

Trends

More passive safety features

Less dependency on active safety systems

Lower core damage frequencies 10 -6

More back up safety systems more trains

S ome core catchers

Larger plants to lower capital cost $/kw

S implification in design

T errorist resistant features

C onstruction time reduced but still long 4 years

ESBWR Design Features

•Natural circulation Boiling Water Reactor

•Passive Safety Systems

•Key Improvements:

Simplification

R educ tion in systems and equipment

R educ tion in operator challenges

R educ tion in core damage frequency

R educ tion in cost/MWe

Reduced flow restrictions

improved separators

shorter core

increase downcomer area

Higher driving head

chimney and taller vessel

Enhanced Natural Circulation

Compared to Standard BWR’s

Enhanced Natural Circulation Compared to Standard BWR’s

8

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Differences relative to ABWR

ABWR

ESBWR

Recirculation System + s upport s ystems

E liminated (Natural Circulation)

HPCF ( H igh Pressure Core Flooder) (2 each)

Combined all ECCS into one G r avity Driven Cooling System (4 divisions)

LPFL (Low Pressure Core Flooder) (3 each)

RCIC ( Isolation/Hi-Pressure s mall break makeup)

Rep l a c e d with IC heat excha nge rs (isolation) and CRD makeup (s mall break makeup)

Residual Heat Removal ( 3 each) (shutdown cooling & containment cooling)

Non-safety shutdown cooling, combined with cleanup system; Passive Containment Coo l ing

Standby Liquid Control System–2 pumps

R ep laced SLCS pumps with accumulators

Reactor Building Service Water ( S afety Grade)

And Plant Service Water (Safety G r ade)

Made non-safety grade o ptimized for Outage duration

Safety Grade Diesel Generators (3 each)

Eliminated only 2 non- s afety grade diesels

9

2 Major Differences N atural Circulation and Passive Safet y

Passive Safety Systems Within Containment Envelope

Decay Heat HX’s Above Drywell

All Pipes/Valves Inside Containment

High Elevation Gravity Drain Pools

Raised Suppre s sion Pool

10

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Fission Research at MIT Nuclear Science and Engineering

Fusion

Fission

NST

NSED

Tracks

CANE S

Centers

Hydrogen

Gen-IV

Fuel cycle

Adv. LWRs

Research foci

Annular fuel Hy dride fuel Nanofluids

NGNP GFR LFR SCWR

Syste m Studies

TRU burning Economics

Projects

11

Annular Fuel for High Power Density PWRs

L arge project lead by MIT (Westinghouse, Gamma Eng.

, Framatome ANP, AECL)

Operates at low peak temperatures (1000 C lower than solid fuel)

F uel allows increase of power density by 50% keeping same TH margins

Allows achievement of burnup of 90MWd/kgHM

12

Appreciably increase of rate of return (economically attractive)

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ADVANTAGES

Thermal Hydraulic Performance: Fuel Temperature

Very low operating peak fuel temperature

2400

2200

2000

Temperatur e o ( C)

1800

1600

1400

1200

As s u mp t i o n s :

S o l i d fuel rod 17x17 , q ' =45k W / m Annular fuel rod 1 5 x15, q'=60kW / m Annular fuel rod 1 5 x15, q'=120k W / m

1000

80 0

60 0

40 0

20 0

- H o t s p ot l i ne a r p o w e r s

-S a m e core pea k i n g of 2 . 5

-S a m e core pow e r for 45kW / m and 60kW / m ca ses

0 1 2 3 4 5 6 7

Rad i us (mm )

MIT Center for Advanced Nuclear Energy Systems 13

Nanofluids P roject

Nano… what? A nanofluid is an ‘engineered’ c olloid = base fluid (water, organic liqu id, gas) + nanoparticles

Nanoparticle s ize: 1-100 nm

Nanoparticle m aterials: Al 2 O 3 , ZrO 2 , SiO 2 , CuO, Cu, Au, C

Critical heat flux increases

Makes nanofluids appealing

for nuclear. Possibility o f significant power dens ity increase.

But large gaps in database and understanding of the

14

enhancement mechanisms exist.

Supercritical CO2 cycle for Gen. IV

A chieves high efficiency at medium temperature

H as ~25% lower cost than Rankine cycle

C O2 abundant, cheap and does not leak as eas ily as helium

I s extremely compact (300MWe turbine fits in home size refrigerator)

A pplicable to reactors with outlet temperature

>500 C (most GenIV reactors)

reactors

PR EC O O L ER

8

8

1

32C

7.7 MPa

FL OW SPL I T

8

MAIN COMPRE SSO R

RE CO MPRE SSING COMPRE S SOR

6

3

FL OW ME RGE

5

3

3

TU R BI N E

650C

20MPa RE ACT OR

2

4

LOW TEM P E RATURE R E CUP ER ATOR

7

8

6

HIGH TEM P E RATURE REC U P E RA TO R

Thermal/net efficiency =51%/ 48%

250MWe steam turbine

300MW S-CO2 turbine 15

Gas Cooled Fast Reactor for Gen IV Service

Wa te r C ooling Heat E x ch an g er

Gu ard Co n t ain m en t

Eme r ge nc y / Shutdown Cooling Heat Exch an g er

Ge ne r a to r

- seal s

- be a r ings

Turbine R e c upe ra t o r

M odule

Bl o w er

C l o sed C h ec k Valve

H i gh Pre s s ure

Open C o mp resso r

C h ec k Valve

Pas siv e/A ct i ve

D eca y H eat Re moval S yst em

Ref l ect o r

600 MW t h CEA

Pl ate- T yp e C o r e

Inte r c oole r M odu le

Pre c oo ler M odule

Low Pre s s u re C o mp resso r

P o w e r Con ver sion U n it

* Not to s c a l e

R eac to r V essel

•Strives to achieve Gen IV go als sustainability, safety and economics

•Allows management of transuranics from LWR spent fuel

a

•Uses combination of active and passive decay heat removal systems (passive based on natural circulation at elevated pressure)

•Direct, highly efficient S-CO2 cycle

•Innovative tube-in-duct fuel assemblies with vibropack (U,TRU)O2 fuel

•Large power rating (1200MWe)

•Breed &Burn core, which does not require reprocessing possible

Pu/TRU

LWR Pu

burner

First Ti er

Second Tier

Fast re actor or Accelerator Driven Sys.

Recycling

MA/TRU

Reproc essing

LWR

Burndo wn

burner

TRU/Pu

Recycling

Pu/TRU

Reproc essing

LWR

Once Through

Repository

Spent fuel

LWR

Fuel Cycle Options

The CONFU Assembly Concept

Co mbined N on - F ertile and U O 2 Assembly

Guide Tubes

Fert ile Free Pins : 70 v/o Spinel ( M g A l 2 O 4 )

U O 2 Pins

18 v/o YSZ

.2% Enrichment

12 v/o (TRU) O 2

Total 13.2 kg of TRU/assembly

M u l t i - r e c y c l i n g o f a l l transuranics ( T R U ) i n f e r t i l e f r e e p i n s l e a d s t o zero net TRU generation

Preserves the cycl e l e ngth, neutronic control and safety features of all uranium cores

Courtesy of Shwageraus, E. Used with permission.

Ņ Optimization of the LWR Nuclear Fuel Cycle for Minimum Waste Production Ó , 38

E. Shwageraus , M.S. Kazimi and P. H e j z l a r , CANES, MIT (2003)

Risk Informed Design, Safety and Licensing

Use PRA principles in design of CO2 gas reactor avoid problems

T echnology neutral risk informed safety standards

“License by test” regulatory approach for innovative reactors

The “Next” Generation

Next Generation Nuclear Plant (NGNP)

N uclear Hydrogen Production

P ebble Bed Reactors H igh Temperature Gas

R isk Informed Design, Safety and Licensing

Next Generation Nuclear Plant

H igh Temperature Gas

Indirect Cycle

E lectric generation

H ydrogen production

P ebble bed reactor or block reactor?

B uilt at the Idaho National Laboratory

Next Generation Nuclear Plant

Hydrogen - T hermo-electric plant

MIT Modular Pebble

Bed Reactor

Secondary HX

Hydrogen - T hermo-chemical plant

Very-High-Temperature Reactor (VHTR)

Characteristics

Helium coolant

1000°C outlet t e mperature

Water-cracking cycle

Benefits

Hy drogen production

High degree of passive safety

High thermal eff i ciency

Process heat applicat ions

U.S. Pro d u ct Team Leader: D r . Fi nis So ut hw orth (INEEL)

23

1150 MW Combined Heat and Power Station

Ten-Unit VHTR Plant Layout (Top View )

(distances in m e ters)

Ad m i n

Equip

9 A c ces s Ha tch

7

Equip

3 A c ces s Ha tch

1

T r aining

10

6

Equip A c ces s Ha tch

4

2

Contr o l Bldg.

Maintenanc e Par t s / T ools

T urbine H a ll Bo u nda ry

Pri m ary is land with r e actor and I H X

Turbo m achinery

8

0 20 40 60 80 100 120 140 1 6 0

5

Desalinization Plant

0

20

40

60

80

10 0

Oil Refinery

VHTR Characteristics

- T emperatures > 900 C

- Indirect Cycle

- C ore Options Available

- Waste Minimization

Hydrogen Production

24

Overview of the efficiency of nuclear hydrogen production options

Approach

Electrochemical

Feature

Water Electroly s is

High Temperature Steam Electroly s is

Thermochemical

Steam-

Meth an e Reformin g

Thermochemica l Water Splitting

Required temperature,

o C

Efficiency of the process,

%

Energy effici ency coupled to LWR, %

Energy effici ency coupled to MHR, ALW R , ATHR, or

S- A G R, %

< 100,

at P atm

>100,

at P atm

> 700

65 8 0

65-95 (200>T>800 0 C)

60-80 (T > 7 00 0 C)

> 800 for S-I WSP

> 700 for UT-3

> 600 for Cu-Cl

> ~40, depending on TC cycle and temperature

21-30

~30

Not Fea s ib le

Not Feasible

21-40

35-45

(Depending on el ect rical cycl e and temperature)

> 60 (T > 7 00 0 C)

>~ 40, depending on TC cycle and temperature

T he hydrogen production efficiency =

LHV for gaseous product/ther mal

energy of fission

reactors

D eviation from ideal

efficiency values can be due to:

heat losses

irreversibilities in the components

25

F inal comparison shou ld take the same conditions into account

Hydrogen Production Energy Efficiency

Comparison of the thermal-to-hydrogen efficiency of the HTSE, SI and WSP related technologies as a function of temperature

26

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Pebble Bed Reactor Research

R eactor physics modeling of core - M CNP

F uel performance model

Safety analysis L OCA and Air Ingress with CFD tools

Pebble Flow modeling and experiments

Balance of plant modularity lego style”

O verall plant conceptual design

N on-proliferation studies

W aste disposal studies

I ntermediate Heat Exchanger design and testing

27

What is a Pebble Bed Reactor ?

360,000 pebbles in core

about 3,000 pebbles handled by FHS each day

about 350 discarded daily

one pebble discharged every 30 seconds

average pebble cycles through core 10 times

Fuel handling most maintenance-intensive part of plant

FU E L E L E M EN T D E S I G N F O R P B M R

5m m Graphi t e l ayer

C o at ed p art ic l es imbedded i n Gr aphi te M at r i x

D i a. 60m m

Py r o l y t i c C ar bon 40 / 1 0 0 0 m m

Fu e l S phe r e

S ilic o n Ca rb it e B a r r ie r C o a t in g 35 / 1 0 0 0

Ha lf S e ct ion

I n ne r Py r o l y t i c Car bon 40 / 1 0 0 0 m m

Po ro us Ca r b o n Bu f f er 9 5/ 1 00 0m m

Di a. 0 , 92m m

Coa t e d P ar t i c le

D i a. 0,5mm U r an ium D i oxi de

Fu el

Reactor Unit

Helium Flowpath

32

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AVR: Jülich

15 MWe R esearch Reactor

HTR- 10 China

First Criticality Dec.1, 2000

China - Rongcheng Site for 19 Pebble Bed Reactors for 3600 Mwe @ 190 Mwe each

Demonstration Plant 35

Features of MIT MPBR Design

Thermal Power

250 MW

Gross Electrical Power

132.5 MW

Net Electrical Power

120.3 MW

Plant Net Efficiency

48.1% (Not take into account cooling IHX and HPT. if considering, it is believed > 45%)

Helium Mass flowrate

126.7 kg/s

Core Outlet/Inlet T

900°C/520°C

Cycle pressure ratio

2.96

Power conversion unit

Three-shaft Arrangement

36

Current Design Schematic

28 0 C

52 0 C

12 6. 7 kg/ s

Reactor core

80 0 C

7. 75 M Pa

79 9. 2 C

HPT 52 .8M W

MPC 2

26.1 MW

HP C 26 .1M W

69 .7 C

8. 0 M Pa

90 0 C

IHX

7. 73 M Pa

6. 44 M P a

Intercool er

69.7 C

4. 67 M Pa

52 2. 5 C

7. 89 M Pa

12 5. 4 kg/ s

11 5 C

1. 3 k g/ s

Cooling RPV

50 9. 2 C

7. 59 M Pa 35 0 C

7. 90 M Pa

Circul ator

32 6 C

10 5. 7 kg/ s

69 .7 C

1. 3 k g/ s

LPT 52 .8M W

71 9. C

5. 21 M Pa

PT 13 6. 9M W

51 1. 0 C

2. 75 M Pa

LP C

26.1 MW

30 C

2. 71 M Pa

MPC 1 26 .1M W

Generator

Bypass Valve

Re cupera tor

96 .1 C

2. 73 M Pa

Precooler

Inventory control

37

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IHX M o dule

Re a c to r Vesse l

R e c u p e ra t o r M o du l e

TOP VIEW WHOLE PLANT

Pla nt Footpr int

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~77 f t .

T u r b oge ne r a to r

MP T u r b ine LP T u r b in e

HP T u rbine

Pr e c o o le r

LP C o m p re ssor

MP Compre ssor

Int e rc o o l e r # 1

~7 0 f t .

P o we r Tu rbi n e HP Compre ssor

I n te r c oo le r #2

38

PLANT MODULE SHIPPING BREAKDOWN

Tot a l M o dul e s N e e d e d F o r P l an t A s s e m b l y ( 2 1 ) : N i n e 8 x3 0 M o dule s , F i v e 8x 4 0 M o dul e s , Se v e n 8x 2 0 M o dul e s

S i x 8x 3 0 I HX M o du l e s Six 8x2 0 R e cu pe r a to r M odu le s

8 x30 Po wer T ur bin e Mo dule

8x2 0 I n ter c o o le r #2 M odu le

8 x40 Piping a nd Pr e c ooler M odu le

8x 30 Upp e r M a n i f o ld Mo dule

8x 30 L owe r Ma nif old Modu le

8x 40 Pip i ng & I n te r c ooler # 1 Mod u le

8x 40 MP T ur b in e, MP Compr e ssor M odu le

8x 4 0 HP Tu rbi n e, L P C o m p re sso r M o du le

8x 4 0 LP T u rb in e , HP C o m p re sso r M o d u l e

39

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Re actor Vessel

IHX Vessel

Present Layout

High Pressure Turbine

Low Pressure Turbine

Compressor (4)

Power Turbine

Re cupera tor V essel

40

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Space-Frame Concept

Standardized Frame Size

2 .4 x 2.6 x 3(n) Meter

Standard Dry Cargo Container

Attempt to Limit Module Mass to

~30t / 6m

I SO Limit for 6m Container

Stacking Load Limit ~190t

I SO Container Mass ~2200kg

Modified Design for Higher Capacity—~60t / 12m module

O verweight Modules

G enerator (150-200t)

T urbo-Compressor (45t)

Avoid Separating Shafts!

H eavy Lift Handling Required

D ual Module (12m / 60t)

Stacking Load Limit Acceptable D ual Module = ~380T

T urbo-generator Module

<300t

D esign Frame for Cantilever Loads Enables Modules to be Bridged

S pace Frames are the structural supports for the components.

O nly need to build open vault areas for space frame installation - RC & BOP vault

Alignment Pins on Module Corners

High Accuracy Alignment

Enables Flanges to be Simply Bolted Together

Standardized Umbilical Locations

Bus-Layout of Generic Utilities

(data/control) 41

Upper IHX Manifold in Spaceframe

3 m

10 m

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2.5 m

42

43

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“Lego” S tyle Assembly in the Field

Overall Structure

25 m

40 m

Asse m bly Contrac t or

Component Fabricator #N

e.g. Turbine M a nufact urer

Component Fabricator #1

e.g. Turbine M a nufact urer

S i t e a n d A s s e m b l y S p e c i f i c a t i o n s

M a n a g e m e n t a n d O p e r a t i o n

C om p o ne nt D e s i g n

S p a c e - F r a m e S pe c i f i c a t i o n

Distributed Production Concept

“M PBR Inc.”

Site Preparation Contrac t or

MPBR Construction Site

Labor

Component Transportati on Design Information

46

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Distributed Production Concept - V irtual Factory !

Evolution of the “Reactor Factory” Concept

T here Is NO Factory

O ff-load Manufacturing Capital Expens e to Component Suppliers

D ecrease follow-through capital expense by des igning to minimize new tooling—near COTS

M ajor component fabricators become mid-level integrators— following design delivered from HQ

R educ es Transportation Costs

C omponent weight Module weight: Why Transport It Twice?

E nables Flexible Capitalization

I nitial systems use components purchased on a one-off / low quantity basis

Once MPBR demand established, constant produc tion + fabrication learning curve lower costs

S ite / Building Des i gn Does Not Require Specialized Expertise E nables Selection of Construc tion Contractors By Location /

Cost

S implified Fabrication Mini mizes “MPBR Inc.” W orkforce Required

S imple Common Space-Frame Design

C an be Easily Manufactured By Each Indiv idual Component Supplier

Or if necessary sub-contracted to generic structural fabricator

M odern CAD/CAE Techniques Enable High First-Fit Probability— Virtual “Test-Fit”

Challenges

U nless the cost of new plants can be substantially reduced, new orders will not be forthcoming.

T he novel truly modular way of building plants may be the right way to go s horter construction times.

S maller units may be cheaper than larger units economies of production may trump the economies of scale when financial risks are considered.

T he bottom line is cents/kwhr not $/kwe ! !

Why Helium Gas? Why Now?

Differences Between Water Reactors

H igher Thermal Efficiencies Possible

H elium inert gas

M inimizes use of water in cycle - c orrosion

S ingle Phase coolant fewer problems in accident

U tilizes gas turbine technology

Lower Power Density no meltdown !

Less Complicated Design (No Emergency Core Cooling Systems Needed)

Lower cost electricity

Generating Cost

PBMR vs. AP600, AP1000, CCGT and Coal

(Comparison at 11% IRR for Nuclear Options, 9% for Coal and CCGT 1 )

AP1000 @

Coal 2

CCGT @ Nat. Gas = 3

AP600

3000Th 3400T h

PBM R

Clean Normal

$ 3 . 0 0 $3. 5 0 $4. 0 0 $10.00

0.5

0.5 0.5

0.48

0.6 0.6

2 . 1 2 . 4 5 2 . 8 7.0

0.8

0.52 0.46

0.23

0.8 0.6

0 . 2 5 0 . 2 5 0 . 2 5 0.25

0.1

0.1 0.1

0.08

- -

- - -

0.1

0.1 0. 1

0.1

- _ - _

- - - _

1.5

1.22 1.16

0.89

1.4 1.2

2 . 3 5 2 . 7 0 3 . 0 5 7.25

3.4

2.5 2. 1

2.2

2.0 1.5

1.0 1.0 1.0 1.0

4.9

3.72 3.26

3.09

3.4 2.7

3 . 3 5 3 . 7 0 4 . 0 5 8.75

(All in ¢ /kWh)

Fue l O&M

Decommissio n i n g F u el Cy cle

Total Op Costs Capital Recovery

Tota l

1 All opti ons exclude property taxes

2 Pr elim inar y bes t c a se c o al opt i ons : mi ne mouth l o c a tio n with $ 20/to n co al , 90 % cap a city fa ctor & 10,000 BTU/k W h heat rate

3 Natural gas price in $/million Btu

51

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Pebble Power Applications

Electricity Direct or Indirect Cycle

high temperature gas turbine

s team cycle using steam generators

Process Heat

H y d rogen h igh temperature thermo-chemical process

D esalinization bottoming cycle

Electricity and Process Heat

Oil Sands

O il Shale

H y d rogen H igh Temperature Steam Electrolys is

O il Production and Refining

C oal G asification and Liquifaction

Drivers for nuclear are CO2 and Economics

Syncrude Plant Site in Alberta

I m age Court e sy of Syncrude

Summary

Main strategic research lines in fission:

1) Improve LWR economics

2) Develop NGNP Plant with Hydrogen Production

2) Develop Gen-IV systems

3) Improve nuclear fuel cycle

4) Global Nuclear Energy Partnership

Fast Neutron Reactors that “burn” waste and breed fuel design course objective

MIT OpenCourseWare http://ocw.mit.edu

22.091 Nuclear Reactor Safety

Spring 200 8

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