Attributable risk function in the proportional hazards model by Chen Y.Q., Hu C., Wang Y.

By Chen Y.Q., Hu C., Wang Y.

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B.. S I I u I Cxl L ~ O'J ,"4 I I O0 I q::) ,-~ ,-~ I ~. i I ~ ~ u2. ~ u2. 9 I ~ C~ C~ c: c: c L~ C C~ oC " ~ OE I C~ C~ Lt:. ~--~ CPC ~ C b- C C I I I I ~t~ I C~ CO I C~ C~ C~ oO ~c) 0 ~ C~C c'O at: ~D c~ b- I C~ I I co oo I I oo~ Lt~ ~ 1 L ~ :~ o c~ I b-. D LO O0 b - q) qp oo oo oo E:) L~ Cxl CO C~1 b - O0 O0 I I I I I I Lt~ o. I LO o. 3 7. 7 3. 7 6. 5 ALL BLACK E O b s e r v e r should s t a n d 3 0 - 3 0 0 m f r o m stack a n d hold scale at a r m ' s length. He should t h e n d e t e r m i n e the shade in the c h a r t m o s t n e a r l y c o r r e s p o n d i n g to the shade of the smoke.

In good practice it is about 20%. 8 t ',t\\kkk\,x 10 uj 9 / f I 8 tD 7 b. k,~o:, \ ' , \ \ 6 \\. ~ ~.. ~ J ' ~ 20 22 24 26 28 30 32 HEAT LOSS AS PER CENT OF CALORIFIC VALUE HEAT LOSS IN FLUE GASES FOR NATURAL GAS i 18 | ~t ttl~ 15 ,\ 13 12 li\ \ ttLkk 17 14 L\ \~ ' , i\ \ \x\ ,r ~,\" \ \;, \\ ,,x,oo~ 10 ~ ~ w - \ \ 9 10 12 . \ 16 . 18 20 22 ~~ ~ 24 26 28 30 32 34 HEAT LOSS AS PER CENT OF CALORIFIC VALUE HEAT LOSS IN FLUE GASES FOR TOWN GAS 36 38 Combustion 35 S e n s i b l e h e a t c a r r i e d a w a y by flue g a s e s i :y 14 _ ~ N.

Dif. Evaporators or Condensers One fluid r e m a i n s at a c o n s t a n t t e m p e r a t u r e while changing its state. s ! 3 log10 ~ ts - tl Mixed Flow One of the fluids takes an irregular direction with respect to the other. tal tm -- -- 2 ta2 tl -- t 2 2 Heat t r a n s f e r in the u n s t e a d y s t a t e N e w t o n ' s L a w o f c o o l i n g . In the w a r m i n g and cooling of bodies, the h e a t gain or loss, respectively, is proportional to the difference b e t w e e n the t e m p e r a t u r e s of the body and the surroundings.

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