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Extra resources for Liquid Metal Engineering Ctr - [semiannual progress rpt Jul-Dec 1969]
TEST AND EVALUATION ACTIVITIES A significant d e p a r t u r e f r o m expected p e r f o r m a n c e w a s noted during o p e r a - tion of the A l c o / B L H s t e a m g e n e r a t o r a t the 40(r0 load l e v e l p r i o r to shutdown i n June 1969. This was manifested a s a d e c r e a s e i n h e a t t r a n s f e r coefficient f o r the boiling r e g i m e . An extensive investigation w a s conducted into possible This w o r k is r e p o r t e d in d e t a i l in Section V I c a u s e s of t h e unexpected behavior.
Above 28,000 gpm, i n d i r e c t o r t b o o t s t r a p c a l i b r a t i o n i s being considered. LMEC- 70- 1 65 14 .. I I OTO 20-in. AP SENSOR I I -- OTO 100-in. ~ I I I - 0 TO 400-in. c AP SENSOR 1 I AP SENSOR 12 10 8 6 ERROR VALUES USED: MAX IM u l l 4 2 0 I I I I I I I I I 2 4 6 8 10 12 14 16 18 FLOWRATE F i g u r e 25.
F o r t h e S P T F to m e e t the a c c u r a c y r e q u i r e m e n t s of l a r g e plant d e s i g n e r s and to c a l i b r a t e f l o w m e t e r s f o r sodium t e s t loops, it will b e n e c e s s a r y to i n s t a l l flow c a l i b r a t i o n capability in the S P T F . The S P T F A - E h a s investigated a weigh c e l l installation on the feed and d r a i n tank P h a s e I1 loop configuration. 770 of instantaneous flow is estimated. Above 28,000 gpm, i n d i r e c t o r t b o o t s t r a p c a l i b r a t i o n i s being considered.