FILTRACJA IZOBARYCZNA |
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objętość [m3] |
czas [s] |
t/V |
V [ml] |
A=0,0712 C |
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y = ax + b |
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0,000050 |
88 |
1,760 |
50 |
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V = K(t/V) - 2C |
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0,000100 |
176 |
1,760 |
100 |
Pomiar absorbancji przed filtracją: |
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a |
42,913 |
K |
42,913 |
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0,000150 |
292 |
1,947 |
150 |
0,183 |
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b |
156,1 |
C |
-78,05 |
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0,000200 |
432 |
2,160 |
200 |
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0,000250 |
607 |
2,428 |
250 |
stąd C1: |
2,570 |
[g/l] |
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0,000300 |
880 |
2,933 |
300 |
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0,000350 |
1240 |
3,543 |
350 |
Absorbancja po filtracji: |
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0,000400 |
1980 |
4,950 |
400 |
0,174 |
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0,000425 |
2983 |
7,019 |
425 |
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stąd C2: |
2,444 |
[g/l] |
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Powierzchnia sączka |
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298,49625 |
300 cm2 |
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y = ax + b |
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0,3 m2 |
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a |
98,788 |
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K1 |
98,788 |
m^6 / s |
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FILTRACJA PRÓŻNIOWA 1 |
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b |
107,42 |
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C1 |
-53,71 |
m^3 |
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objętość [m3] |
czas [s] |
t/V |
V [ml] |
Pomiar absorbancji: |
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0,00010 |
32 |
0,320 |
100 |
0,129 |
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y = ax + b |
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0,00015 |
84 |
0,560 |
150 |
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a |
364,78 |
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K2 |
364,78 |
m^6 / s |
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0,00020 |
170 |
0,850 |
200 |
A=0,0712 C |
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b |
102,15 |
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C2 |
-51,075 |
m^3 |
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0,00025 |
282 |
1,128 |
250 |
stąd C: |
1,812 |
[g/l] |
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0,00030 |
485 |
1,617 |
300 |
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p1 |
0,1 |
atm |
10000 |
Pa |
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0,00035 |
828 |
2,366 |
350 |
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p2 |
0,36 |
atm |
36000 |
Pa |
s = 1 - [ lg (K1/K2) / lg (dp1/dp2) ] |
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0,00040 |
1305 |
3,263 |
400 |
Powierzchnia sączka: |
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153,86 |
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dp1 = p(atm) - p1 |
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dp1 |
90000 |
Pa |
K1 / K2 |
0,270815285925763 |
delta p |
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0,153 m2 |
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dp2 = p(atm) - p2 |
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dp2 |
64000 |
Pa |
dp1 / dp2 |
1,40625 |
0,1 atm |
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log (K1/K2) |
-0,567326825932788 |
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log (dp1/dp2) |
0,148062535455438 |
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s |
4,8316703424516 |
FILTRACJA PRÓŻNIOWA 2 |
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Pomiar absorbancji: |
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objętość [m3] |
czas [s] |
t/V |
V [ml] |
0,144 |
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y = ax + b |
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0,00005 |
8 |
0,16000 |
50 |
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a |
364,78 |
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K2 |
364,78 |
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0,00010 |
20 |
0,20000 |
100 |
A=0,0712 C |
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b |
102,15 |
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C |
-51,075 |
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0,00015 |
27 |
0,18000 |
150 |
stąd C: |
2,022 |
[g/l] |
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0,00020 |
50 |
0,25000 |
200 |
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0,00025 |
95 |
0,38000 |
250 |
Powierzchnia sączka: |
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0,00030 |
155 |
0,51667 |
300 |
153,86 |
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0,00035 |
235 |
0,67143 |
350 |
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0,153 m2 |
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0,00040 |
338 |
0,84500 |
400 |
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delta p |
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0,36 atm |
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