Storage Vessel
Material Balance
Calculations:
                        F3a
Overall Mass Balance:       =F 4                [III.4.1]
                         2
2,600 kg/day
             =1,300 kg /batch
      2
Table III.4.1.1 Summary of Values around Storage Vessel
                             Storage Vessel                             Storage Vessel
    Component                                      Component
                              (Enter)                                        (Exit)
                         Flow Rate (kg/day)                                Flow Rate
                                                                            (kg/day)
 Dried Corn Stover               2,600         Dried Corn Stover             2,600
       Total                     2,600               Total                   2,600
III.4.2. Design Consideration and Selection
For short-term storage of solid materials for the next process, overhead bunkers are
normally used (Sinnot, et al., 2005). Bunkers are also referred to as bins which have two
sections: cylinder and hopper (Carson, 2008). To control the rate of discharge, a valve is
used.
III.4.3. Design Specifications
The specification of the storage vessel and the calculations follows Bulk Solids Handling:
Equipment Selection and Operation by McGlinchey (2008). For the materials of
construction, reinforced concrete is the most common alternative and a double layer of
reinforcing steel is likely to be considered due to concerns such as abrasion and/or
corrosion.  In determining the required size of the bin, first consideration is the mass of
the material then converting it into a volume by estimating the bulk density of the
material to be stored. The common bulk density of dried corn stover is 130
kg
   (Kumar et al . , 2017).
m3
Calculating the volume of dried corn stover:
                        m dried corn stover
V dried corn stover =
                              ρbulk
                         2,600 kg
V dried corn stover =
                        130 kg /m 3
V dried corn stover =20 m3
The general rule of thumb for process vessels, 10% to 15% of the total tank volume
must provide a section for overfill protection to accommodate upsets and also the
working volume of the tank is 80% (Hall, 2018).
Calculating the volume of the cylinder:
               20 m 3
V cylinder =
               0.80
V cylinder =25 m3
Usually, a reasonable and economical height to diameter ratio is between 1.5 to 4.0.
Assuming the economical height to diameter is 2.
H
  =2
D
Calculating the diameter of the cylinder:
V cylinder =π ¿
25 m 3=π ¿
D=0.99 m
Calculating the height of the cylinder:
H=2 D=2(0.99 m)
H=1.98 m