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SIZING OF VESSELS IN
BATCH PLANTS
Sizing Of Vessels In Batch Plants
For sizing of vessels in batch plants we will consider the equipment sizing for
the single product plants, the idea for the sizing is illustrated here by an
example:
Example 1: Single product plant
Assume we have two stage plant and we want to produce 500000 lb/year of
product C. The plant is assumed to operate 6000 hours per year. The recipe of
producing C is as follows:
1) Mixture 1 lb A, 1 lb B and react for 4 hours to form C. The yield is 40% in eight
and the density of the mixture is 60 lb/ft3
2) Add 1 lb solvent and separate by centrifuge during 1 hour to recover 95% of
product C. The density of the mixture is 65 lb/ft3
Sizing Of Vessels In Batch Plants
1 lb solvent
1 lb A 1.2 lb A,B
2.24lb
1 lb B 0.8 lb C A,B, solv.
0.76 lb C
Figure 1: Mass balance for batch plant
Reaction Separation
Sizing Of Vessels In Batch Plants
The specific volume for Stage 1 is V = 1/60 = 0.0166ft3 / lb mix. In this we
have
S1 = 0.0166 * 2 / 0.76 = 0.0438 ft3/lb
Similarly for Stage 2 the specific volume is V= 0.0153ft3/lb mixture. Thus the
size factor is
S2= 0.0153 * 3 / 0.76 = 0.0604 ft3/lb
If we use one unit per stage and operate with zero wait transfer. The cycle
time is
CT = max {4,1} = 4 hrs
This, then implies that the number of batches t be processed in 6000 hrs is
No. Batches = 6000 hrs / 4 hrs per batch = 1500 batches
Sizing Of Vessels In Batch Plants
Since the product demand is 500000 lb the batch size of the final product is
B = 500000 / 1500 = 333lb
We can then easily compute the volume of two vessels :
V1 = S1 B = 0.0438 * 333 = 14.6 ft3
V2 = S2 B = 0.0604 * 333 = 20.1 ft3
Since the bottleneck is in stage 1, we might consider placing two units
operating in parallel out of phase. The cycle time is then
CT = max {4/2,1} = 2 hrs
Sizing Of Vessels In Batch Plants
This implies we can produce twice as many batches 3000 each of 166lb, or
half the original batch size.
In This way the size are as follows:
V1 = 7.3 ft3
V2= 10 ft3
Although the total volume 24.6 ft3 is smaller than the case of 1 unit per stage
34.7 ft3 we require a total of 3 vessels, 2 in Stage 1 and 1 in Stage 2. Depending
on the cost correlation we may or may not achieve reduction in the investment
in the cost.
Sizing Of Vessels In Batch Plants
 Example 2: Multiple product plant
Let us consider a plant consisting of two stages that manufactures two
products A and B. The demand are 500000 lb/year for A and 300000 lb/year for
B and the production time considered is 6000 hrs. Data on processing time size
factors and cleanup time are given in table.
Table 1: Data for sizing Two-Product Plant
Product Processing Times (hr.) Size Factors (ft3/lb prod)
Stage 1 Stage 2 Stage 1 Stage 2
A 8 3 0.08 0.05
B 6 3 0.09 0.04
Cleanup times: 4 hours A to B, B to A
Sizing Of Vessels In Batch Plants
Here, single product campaigns has been consider. The production cycle is
taken as 1000 hrs which implies that over 1 year the cycle will be repeated 6
times.
From Fig. 2 it is clear that the effective time for production in each cycle is 992
hrs.
‫؞‬ 𝑡 𝐴 + 𝑡 𝐵 = 992 hrs. (Eq. 1)
tA tB
4 4
1000 hrs
Figure 2: Time allocation for production of A and B
Sizing Of Vessels In Batch Plants
 The batch size Bi of product i is given by
Bi =
𝑝𝑟𝑜𝑑𝑢𝑐𝑡𝑖𝑜𝑛 𝑖
𝑛𝑜.𝑏𝑎𝑡𝑐ℎ𝑒𝑠 𝑖
=
𝑝𝑟𝑜𝑑𝑢𝑐𝑡𝑖𝑜𝑛 𝑖
𝑡𝑖
/𝐶𝑇𝑖
Here ti and CTi are the total production time and cycle time for each product.
 The production of A and B in each campaign is 500000 / 6 = 83333 lb. and
300000/6 = 50000 lb.
 By equating the batch sizes we get,
83,333
𝑡 𝐴
/8
=
50,000
𝑡 𝐵
/6
𝑡 𝐴 = 2.22 𝑡 𝐵 (Eq. 2)
Sizing Of Vessels In Batch Plants
 From Eq.1 and Eq. 2 we get,
tA = 684 hours , tB = 308 hours
 Hence, BA = BB = 974 lb.
 From the batch size the required volumes for each product in two stage can
be calculated by
Vij=SijB
Volumes Vij (ft3)
Product Stage 1 Stage 2
A 77.9 48.7
B 87.7 39.0
Sizing Of Vessels In Batch Plants
 Finally the largest volume to be selected in each stage are given by
Vj = max {Vij}
So, V1 =87.7ft3 , V2 = 48.7ft3
Reference
 Systematic Methods of Chemical Process Design By Lorenz T. Biegler/
Ignacio E. Grossmann / Arthur W. Westerberg
Thank You

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Sizing of vessels in batch plants

  • 1. SIZING OF VESSELS IN BATCH PLANTS
  • 2. Sizing Of Vessels In Batch Plants For sizing of vessels in batch plants we will consider the equipment sizing for the single product plants, the idea for the sizing is illustrated here by an example: Example 1: Single product plant Assume we have two stage plant and we want to produce 500000 lb/year of product C. The plant is assumed to operate 6000 hours per year. The recipe of producing C is as follows: 1) Mixture 1 lb A, 1 lb B and react for 4 hours to form C. The yield is 40% in eight and the density of the mixture is 60 lb/ft3 2) Add 1 lb solvent and separate by centrifuge during 1 hour to recover 95% of product C. The density of the mixture is 65 lb/ft3
  • 3. Sizing Of Vessels In Batch Plants 1 lb solvent 1 lb A 1.2 lb A,B 2.24lb 1 lb B 0.8 lb C A,B, solv. 0.76 lb C Figure 1: Mass balance for batch plant Reaction Separation
  • 4. Sizing Of Vessels In Batch Plants The specific volume for Stage 1 is V = 1/60 = 0.0166ft3 / lb mix. In this we have S1 = 0.0166 * 2 / 0.76 = 0.0438 ft3/lb Similarly for Stage 2 the specific volume is V= 0.0153ft3/lb mixture. Thus the size factor is S2= 0.0153 * 3 / 0.76 = 0.0604 ft3/lb If we use one unit per stage and operate with zero wait transfer. The cycle time is CT = max {4,1} = 4 hrs This, then implies that the number of batches t be processed in 6000 hrs is No. Batches = 6000 hrs / 4 hrs per batch = 1500 batches
  • 5. Sizing Of Vessels In Batch Plants Since the product demand is 500000 lb the batch size of the final product is B = 500000 / 1500 = 333lb We can then easily compute the volume of two vessels : V1 = S1 B = 0.0438 * 333 = 14.6 ft3 V2 = S2 B = 0.0604 * 333 = 20.1 ft3 Since the bottleneck is in stage 1, we might consider placing two units operating in parallel out of phase. The cycle time is then CT = max {4/2,1} = 2 hrs
  • 6. Sizing Of Vessels In Batch Plants This implies we can produce twice as many batches 3000 each of 166lb, or half the original batch size. In This way the size are as follows: V1 = 7.3 ft3 V2= 10 ft3 Although the total volume 24.6 ft3 is smaller than the case of 1 unit per stage 34.7 ft3 we require a total of 3 vessels, 2 in Stage 1 and 1 in Stage 2. Depending on the cost correlation we may or may not achieve reduction in the investment in the cost.
  • 7. Sizing Of Vessels In Batch Plants  Example 2: Multiple product plant Let us consider a plant consisting of two stages that manufactures two products A and B. The demand are 500000 lb/year for A and 300000 lb/year for B and the production time considered is 6000 hrs. Data on processing time size factors and cleanup time are given in table. Table 1: Data for sizing Two-Product Plant Product Processing Times (hr.) Size Factors (ft3/lb prod) Stage 1 Stage 2 Stage 1 Stage 2 A 8 3 0.08 0.05 B 6 3 0.09 0.04 Cleanup times: 4 hours A to B, B to A
  • 8. Sizing Of Vessels In Batch Plants Here, single product campaigns has been consider. The production cycle is taken as 1000 hrs which implies that over 1 year the cycle will be repeated 6 times. From Fig. 2 it is clear that the effective time for production in each cycle is 992 hrs. ‫؞‬ 𝑡 𝐴 + 𝑡 𝐵 = 992 hrs. (Eq. 1) tA tB 4 4 1000 hrs Figure 2: Time allocation for production of A and B
  • 9. Sizing Of Vessels In Batch Plants  The batch size Bi of product i is given by Bi = 𝑝𝑟𝑜𝑑𝑢𝑐𝑡𝑖𝑜𝑛 𝑖 𝑛𝑜.𝑏𝑎𝑡𝑐ℎ𝑒𝑠 𝑖 = 𝑝𝑟𝑜𝑑𝑢𝑐𝑡𝑖𝑜𝑛 𝑖 𝑡𝑖 /𝐶𝑇𝑖 Here ti and CTi are the total production time and cycle time for each product.  The production of A and B in each campaign is 500000 / 6 = 83333 lb. and 300000/6 = 50000 lb.  By equating the batch sizes we get, 83,333 𝑡 𝐴 /8 = 50,000 𝑡 𝐵 /6 𝑡 𝐴 = 2.22 𝑡 𝐵 (Eq. 2)
  • 10. Sizing Of Vessels In Batch Plants  From Eq.1 and Eq. 2 we get, tA = 684 hours , tB = 308 hours  Hence, BA = BB = 974 lb.  From the batch size the required volumes for each product in two stage can be calculated by Vij=SijB Volumes Vij (ft3) Product Stage 1 Stage 2 A 77.9 48.7 B 87.7 39.0
  • 11. Sizing Of Vessels In Batch Plants  Finally the largest volume to be selected in each stage are given by Vj = max {Vij} So, V1 =87.7ft3 , V2 = 48.7ft3
  • 12. Reference  Systematic Methods of Chemical Process Design By Lorenz T. Biegler/ Ignacio E. Grossmann / Arthur W. Westerberg Thank You