Simulation of Ammonia Plant Using Hysys
SIMULATION OF AN INDUSTRIAL SCALE AMMONIA PLANT USING HYSYS™
Presented By
Mohammad Shamsus Saleheen
#0602001 Md. Abu Abdullah Al Hasanat #0602002
1
Outline of the Presentation
Objectives Simulating an ammonia plant using Aspen HYSYS A simplified block diagram of Haldor Topsoe ammonia production process Steady-state Model Comparison of steady-state simulation results with real plant data Response of the Model to Changes in Process Variables Scope of future work
2
Objectives
Building a steady-state model of an industrial scale ammonia plant Comparison of simulation model performance with real plant To study the variation of performance of the plant on some specific variables
3
Simulating an Ammonia Plant Using Aspen HYSYS
Creating a component list
1.
2. Selection of an appropriate Fluid property model 3. Creating Reaction Set
4. 5.
Modeling of the primary reformer Developing the model of ammonia synthesis loop
4
A Simplified Block Diagram of Haldor Topsoe Process
5
Steady-State Model
6
Comparison of Steady-State Simulation Results with Real Plant Data
Variables Product flow rate, kg/hr NH3 % in Product PRF outlet temperature ⁰C H2/N2 after shift convertor PRF outlet composition of CH4 (%) Plant Data 1078 kg/hr 99.34 796 2.896 6.65 Simulation Data 1080 kg/hr 95.26 807.4 2.806 5.85 Deviation from Plant Data, % 0.18553 4.10710 1.43216 3.10773 12.0300
Source: Real plant data obtained from Jamuna Fertilizer Company Ltd, Jamalpur
7
Comparison of Steady-State Simulation Results with Real Plant Data
Product ammonia flow rate(1000 NM3/hr) JFCL HYSYS Model 1078 1080
Product ammonia percentage 99.34 95.26
H2/N2 after shift converter 2.896 2.806
PRF outlet temperature (°C) 796 807.4
Source: Real plant data obtained from Jamuna Fertilizer Company Ltd, Jamalpur
8
Response of the Simulation Model to Changes in Process Variables
Effect of 5% change in Converter Feed
Presented By
Mohammad Shamsus Saleheen
#0602001 Md. Abu Abdullah Al Hasanat #0602002
1
Outline of the Presentation
Objectives Simulating an ammonia plant using Aspen HYSYS A simplified block diagram of Haldor Topsoe ammonia production process Steady-state Model Comparison of steady-state simulation results with real plant data Response of the Model to Changes in Process Variables Scope of future work
2
Objectives
Building a steady-state model of an industrial scale ammonia plant Comparison of simulation model performance with real plant To study the variation of performance of the plant on some specific variables
3
Simulating an Ammonia Plant Using Aspen HYSYS
Creating a component list
1.
2. Selection of an appropriate Fluid property model 3. Creating Reaction Set
4. 5.
Modeling of the primary reformer Developing the model of ammonia synthesis loop
4
A Simplified Block Diagram of Haldor Topsoe Process
5
Steady-State Model
6
Comparison of Steady-State Simulation Results with Real Plant Data
Variables Product flow rate, kg/hr NH3 % in Product PRF outlet temperature ⁰C H2/N2 after shift convertor PRF outlet composition of CH4 (%) Plant Data 1078 kg/hr 99.34 796 2.896 6.65 Simulation Data 1080 kg/hr 95.26 807.4 2.806 5.85 Deviation from Plant Data, % 0.18553 4.10710 1.43216 3.10773 12.0300
Source: Real plant data obtained from Jamuna Fertilizer Company Ltd, Jamalpur
7
Comparison of Steady-State Simulation Results with Real Plant Data
Product ammonia flow rate(1000 NM3/hr) JFCL HYSYS Model 1078 1080
Product ammonia percentage 99.34 95.26
H2/N2 after shift converter 2.896 2.806
PRF outlet temperature (°C) 796 807.4
Source: Real plant data obtained from Jamuna Fertilizer Company Ltd, Jamalpur
8
Response of the Simulation Model to Changes in Process Variables
Effect of 5% change in Converter Feed