22.033 Cor e Gr oup - R eact or Cor e an d Seco ndary Design
R obert Dr enkhahn Br endan Ensor Jessic a Hammond Ruaridh Macdonal d
1
Ov er vie w
• Pr oposed Des ign & Specs
• Cor e
• Sec ondar y
• Ne x t St ep s
2
Pr eliminar y Design
• Lead Cooled F as t R eact or wit h Super crit ic al CO 2 Sec ondar y Loop
• 1000 MWt (~450 M W e )
– Limi t ed b y v elocity of LBE (2.5 - 3 m/ s) curr en tly w e ar e u sin g 2.5 m/ s
– Subject t o c hang es as Δ T and flo w ar ea chang es (w orki ng on up pi ng it t o ~1200 M Wt )
3
Pr eliminar y Design
• Blac k - Fuel R eg i ons ( UO 2 )
• P urple- Con tr ol R ods (B 4 C)
• Be i g e - R e flect or (MgO )
• R ed - Shield (B 4 C)
• Or ange - Cool an t (LBE)
• Not e the B l ue c on t ainment i s not the a c tual c on t ainment (i n r ea l i ty i t i s l ar g er)
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Pr eliminar y Design
• Pict ur e of Whole S y s t em
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Cor e Design Pr ocess
• Us ed M CN P (Mon t e Carlo N - P arti cle) c ode t o desi gn r eact or
• Based of f of o ther si mil ar he x ag on c or e shaped li quid me t al c ooled r eact or s (S T AR - LM, ELS Y)
• Des ign It er a ti ons
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It er a tio n 1
• V er sion 1 .0, loo k ed a t a lo t of r e f er ence design s a nd cr ea t ed some thing similar
• Se e if it w er e cr iti c al
• Fue l Pin de sign: fu el LBE g ap pr ot ect iv e clad T9 1
pr ot ect iv e clad c oo lan t
• It had the whol e r ang e o f S/D wit h r ods in and su per crit ic al wit h r ods out
– Need ed less r eacti vity a t t o p o f c o r e ( help s with S/ D mar gin)
– Ne ede d less po w er peaking in th e mid dle
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It er a tio n 1
Con tr o l R o d s |
K e ff ( + - 0. 0005) |
In |
0. 96822 |
2 5 % out |
1. 01184 |
5 0 % out |
1. 08764 |
7 5 % out |
1. 11812 |
Ful l Out |
1. 3265 |
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It er a tio n 2
• Ad ded Axi al Z onin g t o fix the lar g e e x cess r eactivit y (20 % enriched Low e r , 15% enrich ed Mid dle, 10% enrich ed bot t om)
• Add ed Radial Z oning t o g e t a fla t t er flux pr ofil e (Added 5% t o the out er ri ngs)
Con tr ol R od s |
In |
0.25 |
0.5 |
0.75 |
Out |
Ke f f |
0.953 87 |
1.080 59 |
1.150 39 |
1.161 42 |
1.161 44 |
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It er a tio n 2
• Blac k - Fuel R eg i ons ( UO 2 )
• P urple- Con tr ol R ods (B 4 C)
• Be i g e - R e flect or (MgO )
• R ed - Shield (B 4 C)
• Or ange - Cool an t (LBE)
• Blue - Cladding (T 91 s t ainl es s s t ee l , pr ot ecti v e out er l a y er)
• Not e the B l ue c on t ainment i s not the a c tual c on t ainment (i n r ea l i ty i t i s l ar g er)
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It er a tio n 2
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It er a tio n 2
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P o w er Calcula tion
• Use d P o w er = ṁ c p Δ T
• Wh er e ṁ = ρ v A
• Wh er e v is li mit ed a t 2.5 m/ s, rho is 10500 k g /m 3
, A i s the cr oss se ctional c oolan t fl o w a r ea, c p is 150 J/ kg·K and Δ T i s t he t emp er a tur e chang e acr oss the c or e
• Dir ectl y pr oportion al t o A and Δ T
13
Dec a y Hea t R emov al
• Aft er a mon th of shut do wn fr om long oper a tion s til l pr oducin g about 3 MWt of ener gy
• Aft er a mon th of shut do wn fr om 1 mon th of oper a tion s til l pr oducin g 400 kWt of ener gy
• Ne ed t o see ho w m uch p o w er pr oduced i s suf fi cie n t t o k ee p LBE liq ui d and then w ork with pr ocess h ea t
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Sec ondary S y s t em
• Model ed i n EE S
– T emper a tur e and mass flo w c alcula tion s
• Ini ti al As sum p ti ons Made
– Hea t e x chang er i npu t and outpu t f or S - C O 2
– Low end t emper a tur e aft er c onden ser
• Al lo w s f or f as t er op ti mi z a ti on in th e futu r e
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Sec ondary S y s t em
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Sec ondary S y s t em
• Mor e S - CO 2 da t a r equir ed t o perf orm analy sis of pr essur e chang es.
– En thalp y T able s
• P ossi ble sec ond loo p with an added r e - hea t er and c ompr essor t o a cc oun t f or chang es in specifi c hea t
• Ener gy div ert ed t o Pr ocess - Hea t needs t o be acc oun t ed f or
– On ly majorly e f f ec ts electric ity g ener a t ed
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Q ui c k T i m e™ and a dec om pr e s s or
ar e needed t o s ee t hi s pi c t ur e .
Br a y t on Cy cle: Quick Ov er vie w
Source: UC Davis ChemWiki, license CC BY-NC-SA 3.0
h tt p :/ /ch e m w iki.u cd av is .e d u /@ap i/d e ki/fi le s /132 3 5/ = T S _ Cur v e .jp g
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Q uic k T im e™ and a dec o m pr e s s or
ar e needed t o s ee t his pic t ur e .
LBE & S- C O 2 Hea t Ex chang er
© Heatric. All rights reserved. This content is excluded from o ur Creative Commons license. For more information, see http://ocw.mit.edu/fairuse .
h tt p ://w w w .h e atr i c .c o m/
• Pr in t ed Ci r cuit Hea t Ex chang er (PCHE) v s. Shel l -
and - T ub e Hea t Ex chang er
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PCHE
• Compac t design
• Competitiv e E f ficie ncy
• Fric tion F ac t or f or LBE bec omes ob s t ac le
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She ll - and - T ube Hea t E x chang er
• Simpl e design (ea s y t o mak e, lo w c os t, e t c. )
Q ui c k T i m e™ and a dec om pr e s s or
ar e needed t o s ee t hi s pi c t ur e .
• La r g er than PCHE
• Competi tiv e e f ficiency
© Sulzer Chemtech USA, Inc. All rights reserved. This content is excluded from our Creative Commons license. For more information, see http://ocw.mit.edu/fairuse .
http://www.thermopedia.com/content/1211/?tid=104&sn=1410
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Ne xt St ep
• Sec ondary: Be t t er da t a, mor e accur a t e v alues , possi ble sec ond r e - hea t er/ c om pr essor loop, and pr ocess hea t r emo v al
• Cor e: Na tur al Cir cula ti on, Dec a y hea t w ork, c on ti nue op ti mi zi ng c or e z onin g , the rmal analy si s of f uel
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QUE S TIONS?
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MIT OpenCourseWare http://ocw.mit.edu
22.033 / 22.33 Nuclear Systems Design Project
Fa ll 2011
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