chapter 3 batch processes

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Chapter 3 Batch Processing Department of Chemical Engineering West Virginia University R. Turton and J. A. Shaeiwitz - Copyright 2012 1

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Page 1: Chapter 3   batch processes

Chapter 3 Batch Processing

Department of Chemical Engineering

West Virginia University

R. Turton and J. A. Shaeiwitz - Copyright 2012 1

Page 2: Chapter 3   batch processes

Outline

• Design Calculations

• Gantt Charts and Scheduling

• NonOverlapping and Overlapping Operations

• Cycle Times

• Flowshop Plants

• Jobshop Plants

R. Turton and J. A. Shaeiwitz - Copyright 2012 2

Page 3: Chapter 3   batch processes

Outline

• Product and Intermediate Storage

• Parallel Process Units

• Equipment Design for Multiproduct Batch Processes

R. Turton and J. A. Shaeiwitz - Copyright 2012 3

Page 4: Chapter 3   batch processes

Outline

• Design Calculations

• Gantt Charts and Scheduling

• NonOverlapping and Overlapping Operations

• Cycle Times

• Flowshop Plants

• Jobshop Plants

R. Turton and J. A. Shaeiwitz - Copyright 2012 4

Page 5: Chapter 3   batch processes

Design Calculations

• Recipe

• Operations are unsteady state

• Often existing equipment is used – not designed specifically for recipe

• Transfer from equipment and cleaning important

• Recycling and energy integration issues

R. Turton and J. A. Shaeiwitz - Copyright 2012 5

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Recipe

Step 1: 500 kg of reactant A (MW = 100 kg/kmol) is added to 5000 kg of

a mixture of organic solvent (MW = 200 kg/kmol) containing 60% excess

of a second reactant B (MW = 125 kg/kmol) in a jacketed reaction vessel

(R-301), the reactor is sealed, and the mixture is stirred and heated (using

steam in the jacket) until the temperature has risen to 95C. The density of

the reacting mixture is 875 kg/m3 (time taken = 1.5 h).

Step 2: Once the reaction mixture has reached 95C, a solid catalyst is

added, and reaction takes place while the batch of reactants is stirred. The

required conversion is 94% (time taken = 2.0 h).

Step 3 ……..

Step 4 ……..

Step 5 ……...

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Design Calculations

Because reactors of this sort come in standard sizes, a 3000-gallon (Vtank) reactor is selected.

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3

3

5500[kg]6.286

875[kg/m ]V m

3

3

5500[kg] 110.48 2768

0.6875[kg/m ]requiredV m gal

60% fill

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Design Calculations

R. Turton and J. A. Shaeiwitz - Copyright 2012 8

p s

dTVC UA T T

dt

pos

finals

VC

tUA

TT

TT

ln

Find the time to heat vessel contents from ambient to 95C

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Design Calculations

• Transfer from equipment and cleaning important

Gravity drain or pump

Cleaning – GMP/documentation

• Recycling and energy integration issues

Recycling – often use dump tank and accumulate material from several runs

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Page 10: Chapter 3   batch processes

Outline

• Design Calculations

• Gantt Charts and Scheduling

• NonOverlapping and Overlapping Operations

• Cycle Times

• Flowshop Plants

• Jobshop Plants

R. Turton and J. A. Shaeiwitz - Copyright 2012 10

Page 11: Chapter 3   batch processes

Gantt Charts and Scheduling

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Outline

• Design Calculations

• Gantt Charts and Scheduling

• NonOverlapping and Overlapping Operations

• Cycle Times

• Flowshop Plants

• Jobshop Plants

R. Turton and J. A. Shaeiwitz - Copyright 2012

Page 13: Chapter 3   batch processes

NonOverlapping and Overlapping Operations

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1

m

NO i

i

T n t

Page 14: Chapter 3   batch processes

NonOverlapping and Overlapping Operations

R. Turton and J. A. Shaeiwitz - Copyright 2012 14

Page 15: Chapter 3   batch processes

NonOverlapping and Overlapping Operations

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m

i

iimi

O ttnTT1

,...,1)(max)1(

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Outline

• Design Calculations

• Gantt Charts and Scheduling

• NonOverlapping and Overlapping Operations

• Cycle Times

• Flowshop Plants

• Jobshop Plants

R. Turton and J. A. Shaeiwitz - Copyright 2012

Page 17: Chapter 3   batch processes

Cycle Times

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1,

1

m

i mNO i

cycle NO i

i

n tT

t tn n

n

ttn

n

Ttt

m

i

iimi

cycleOcycle

1,...,1

,

)(max)1(

tcycle = total time/number of batches

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Cycle Times

From the overlapping scheme – when the number of batches (n) to be produced is large,

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1,..,max { }cycle i

i mt t

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Cycle Times

Example

A batch process involves 4 pieces of equipment with the following process times

Heating and Mixing 2.5 h

Reaction 3.5 h

Filtration and Drying 1.5 h

Crystallization and packaging 2.0 h

Determine the cycle times for non-overlapping and overlapping operation.

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Cycle Times

Example

TNO = 2.5+3.5+1.5+2.0 = 9.5 h TO,5 = [(5-1)×3.5+9.5]/5 = (14+9.5)/5 = 4.7 h TO,10 = [(10-1)×3.5+9.5]/5 = (31.5+9.5)/10 = 4.1 h TO,∞ = 3.5 h

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Outline

• Design Calculations

• Gantt Charts and Scheduling

• NonOverlapping and Overlapping Operations

• Cycle Times

• Flowshop Plants

• Jobshop Plants

R. Turton and J. A. Shaeiwitz - Copyright 2012

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Multiple Products

When we have multiple products that can be produced in the same equipment, the scheduling of multiple batches requires careful planning

The different products may require the same processing steps, or more often will require only a subset of all possible steps. Moreover, the order in which a batch process uses different equipment might also differ from product to product

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Flowshop Plants

If all the products use the same equipment in the same order or sequence, but not necessarily for the same lengths of time then the plant is referred to as a flowshop plant

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Flowshop Plants

Consider 3 products A, B, C each requiring to be run nA, nB, and nC times in a given period.

When we want to produce multiple products using the same

equipment then we can either:

• run campaigns of the same product followed by campaigns of the next product followed by……

i.e., run A - nA times followed by B - nB times followed by C -nC times - AAAAAAAABBBBBBBBCCCCCCC

• Intermingle the products so that we run ABCABCABC… or

ACBACBACB…, or AABCAABCAABC

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Flowshop Plants

For multiple- (single) product campaigns the total processing time, or production cycle time, is found by adding the operation times for each product. If the number of batches per campaign is large (for example, >10), then the production cycle time can be approximated by

1,..,

max { }

C C

j cycle j ij i m jj A j A

T n t n t

R. Turton and J. A. Shaeiwitz - Copyright 2012

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Flowshop Plants

Example – production of three products A, B, and C

Use Single Product Campaigns

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Flowshop Plants

What if we want to run as ABCABCABC. What is the cycle time and how many batches can we produce of each product in 500h?

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Flowshop Plants

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Flowshop Plants

3.5h not 2.5 h

Cycle times > 10.5h

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Jobshop Plants

When not all products use the same equipment or the sequence of using the equipment is different for different products, then the plant is referred to as a jobshop plant.

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Jobshop Plants

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Jobshop Plants

For running sequential (multiple) single-product campaigns, the cycle time and number of batches can be determined by the same method used for the flowshop plant.

For sequential operation of batches ABCABC.. or ACBACB… we need to draw the Gantt chart.

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Jobshop Plants

For equal batches of A, B, and C how many batches can be produced in 500 h?

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Jobshop Plants

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Jobshop Plants

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Jobshop Plants

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Jobshop Plants

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Outline

• Product and Intermediate Storage

• Parallel Process Units

• Equipment Design for Multiproduct Batch Processes

R. Turton and J. A. Shaeiwitz - Copyright 2012

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Product Storage

Product Storage for Single-Product Campaigns When using combinations of single-product campaigns in a multi-product plant, it is necessary to store product during the campaign. The amount of storage is dependent on the rate of production and rate of demand for each product and the cycle time.

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Product Storage

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Product Storage

s p d rampV r r t

Rate of production Rate of demand

Campaign time

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Product Storage

For products A, B, and C, determine the minimum storage capacities for a single-product campaign strategy. Assume that 1 month = 500 hours. Note that 43 batches of each unit are required for each product per month.

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Product Storage

Product A (0.093 – 0.020)(43×2.5) = 7.85 m3

B (0.07752 – 0.06202)(43×4.5) = 9.20 m3

C (0.06202 – 0.024)(43×4.5) = 7.36 m3

s p d rampV r r t

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Intermediate Storage

For Multi-product Campaigns

So far, assumed no intermediate product storage available. This type of process is a zero wait, or a zw-process.

Flow to equipment directly from previous equipment in recipe.

Delay in one step propagates through batch to all steps.

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Intermediate Storage

It may be possible to store product in the equipment that has just been used. e.g. if two feed streams are mixed in a vessel, the mixture could be stored until the next process unit in the production sequence becomes available. This holding-in-place method may not work for some unit operations, e.g. in a reactor. The upper limit of the intermediate storage concept occurs when there is unlimited intermediate storage (uis) available, and this is referred to as a uis-process.

R. Turton and J. A. Shaeiwitz - Copyright 2012

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Intermediate Storage

Limiting Case

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Intermediate Storage A B C

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Outline

• Product and Intermediate Storage

• Parallel Process Units

• Equipment Design for Multiproduct Batch Processes

R. Turton and J. A. Shaeiwitz - Copyright 2012

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Parallel Process Units

Reduce bottlenecks caused by a single piece of equipment by duplicating the equipment.

Trade-off between added equipment (and maintenance) cost vs. higher throughput.

Makes sense when one equipment dominates cycle time.

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Parallel Process Units

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A B C

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Outline

• Product and Intermediate Storage

• Parallel Process Units

• Equipment Design for Multiproduct Batch Processes

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Equipment Design for Multi-product Batch Processes

The design of equipment sizes for multiproduct batch processes depends on the

• Production cycle time

• Whether single- or multi-product campaigns are used

• The sequence of products for multi-product campaigns,

• Use of parallel equipment.

R. Turton and J. A. Shaeiwitz - Copyright 2012

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Equipment Design for Multi-product Batch Processes

Example

Clearly the reactor is the limiting piece of equipment – determine the size of the reactor required.

R. Turton and J. A. Shaeiwitz - Copyright 2012

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Equipment Design for Multi-product Batch Processes

From the recipe for each batch, calculations for the specific volume of each reactor can be made – see Chapter 3.

Equations required

Total time for batches tA + tB + tC = 500

Reactor volumes VA = VB = VC

total time taken to produce A

R. Turton and J. A. Shaeiwitz - Copyright 2012