Table 4.
n1 | n2 | J |
|
||||
---|---|---|---|---|---|---|---|
0.5 | 1 | 3 | 5 | ||||
10 | 10 | 0.2 | 0.9510 | 0.9355 | 0.9640 | 0.9695 | |
0.4 | 0.9535 | 0.9540 | 0.9590 | 0.9575 | |||
0.6 | 0.9670 | 0.9655 | 0.9510 | 0.9515 | |||
0.8 | 0.9580 | 0.9615 | 0.9585 | 0.9565 | |||
0.9 | 0.9415 | 0.9470 | 0.9450 | 0.9465 | |||
20 | 20 | 0.2 | 0.9420 | 0.9125 | 0.9410 | 0.9455 | |
0.4 | 0.9455 | 0.9340 | 0.9355 | 0.9315 | |||
0.6 | 0.9535 | 0.9550 | 0.9415 | 0.9335 | |||
0.8 | 0.9530 | 0.9535 | 0.9470 | 0.9405 | |||
0.9 | 0.9345 | 0.9330 | 0.9320 | 0.9290 | |||
10 | 30 | 0.2 | 0.9410 | 0.9200 | 0.9435 | 0.9500 | |
0.4 | 0.9455 | 0.9400 | 0.9295 | 0.9335 | |||
0.6 | 0.9570 | 0.9575 | 0.9485 | 0.9415 | |||
0.8 | 0.9475 | 0.9495 | 0.9430 | 0.9415 | |||
0.9 | 0.9420 | 0.9385 | 0.9350 | 0.9290 | |||
50 | 50 | 0.2 | 0.9255 | 0.8870 | 0.9465 | 0.9460 | |
0.4 | 0.9170 | 0.9135 | 0.9365 | 0.9350 | |||
0.6 | 0.9395 | 0.9515 | 0.9505 | 0.9350 | |||
0.8 | 0.9445 | 0.9455 | 0.9415 | 0.9360 | |||
0.9 | 0.9260 | 0.9280 | 0.9265 | 0.9245 | |||
100 | 100 | 0.2 | 0.9150 | 0.8855 | 0.9250 | 0.9250 | |
0.4 | 0.9150 | 0.9120 | 0.9145 | 0.9185 | |||
0.6 | 0.9400 | 0.9440 | 0.9385 | 0.9250 | |||
0.8 | 0.9335 | 0.9425 | 0.9330 | 0.9275 | |||
0.9 | 0.9270 | 0.9345 | 0.9275 | 0.9220 |
The mixture model is defined as where Bi ~ Bernoulli(0.1) for i = 1, 2.