BLBS102-c38 BLBS102-Simpson March 21, 2012 14:17 Trim: 276mm X 219mm Printer Name: Yet to Come
738 Part 7: Food Processing
Table 38.7.Procedure in Calculation of Process Time Using Ball Method for Conductive
Heating Food
Process Time Calculation
1 jh 1.41
2 fh 60 min
3 Retort temperature (Tr) 245 ◦F
4z(◦F) value 18 ◦F
5 Lethality(Fo)5min
6 CUT 8min
7 Initial product temperature (Ti) 170 ◦F
8Ih=Tr−Ti 75 ◦F= 245 − 170
9jh∗Ih 105.75=1.41∗ 75
10 Log(jh∗Ih) 2.024
11 Fi= 10
( 250 −Tr
z
)
1.9= 10 (
250 − 18245 )
12 fh/U=fh/(Fo∗Fi)fh/U=60/(1.9∗5)=6.32
13 Logg From Ball Table 38. 6 by interpolation=0.821
14 Log(jh.Ih)−logg 1.203=2.024−0.821
15 B=fh[log(jh∗Ih)−log g)] 72.18 min= 60 ∗1.203
16 Pt=B−42%CUT 68.82 min=72.18−0.42∗ 8
conservative assumption from safety point of view but
from quality point of view it has an over processing ef-
fect. In practice, most of the heating is done with steam or
agitated water, while cooling is normally done in slowly
circulating water. Therefore, generallyfh<fcandfh=fc
gives a more conservative processing conditions.
- The temperature difference between the retort temper-
ature and cooling water temperature (Tr−Tcw)isthe
driving force. This is expressed in terms ofIc, which is
(Ic=Tic−Tcw). Ball assumed that the sum ofIc+g=
Tr−Tcw= 180 ◦F (for steam) or 130◦F (for full
immersion water overpressure). Stumbo (1973) discov-
ered that, a 10◦F change inTr−Tcwcan result in 1% dif-
ference in calculated lethality (F 0 ) and can be corrected if
required.
- CUT correction forjhvalue. Ball noticed that only about
42% of the CUT can be considered as effective contribu-
tion to the process time. - No further product heating after cooling starts. However,
this is not always valid for the critical point of conduc-
tion in heated canned foods. In such cases, considerable
overprocessing can occur.
Table 38.8.Calculation of Process Lethality Using Ball Method From Hypothetical Given Data
Process Time Calculation
1 jh 2.05
2 fh 34.9 min
3 CUT 8min
4Pt 45 min
Process time B=Pt+42%CUT
5(B=Pt+42%CUT) B= 45 +0.42∗ 8 =48.36min
6 Retort Temperature (Tr) 260 ◦F
7 Initial temperature(Ti) 100 ◦F
8Ich=Tr−Ti 160 ◦F= 260 − 100
9jh∗Ich 328 ◦F=2.05∗ 160
10 log (jh∗Ih) 2.52
11 zvalue 18 ◦F
12 Fi= 10 (
250 −zTr)
0.278
13 B/fh 1.39=48.36/34.9
14 logg=log(jh∗Ih)−B/fh logg=1.13=2.52−1.39
15 fh/U From Ball Table 38.6 by interpolation=22.4
16 Fo=(fh/Ufh∗Fi) Fo=34.9/(22.4∗0.278)=5.60 min