PRODUCTION OF AN EXISTING 800 TONNES GASES OF A COAL-FIRED POWER PLANT
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1 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, ENHANCING THE OPERATION AND PRODUCTION OF AN EXISTING 800 TONNES PER DAY PLANT CAPTURING CO 2 FROM FLUE GASES OF A COAL-FIRED POWER PLANT Dr. Ahmed Aboudheir, P.Eng. President, Delta Purification, Regina, SK, Canada Dr. Walid ElMoudir, PE P.Eng. Senior Process Engineer, HTC CO 2 Systems, Regina, SK, Canada
2 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Searles Valley Minerals, SVM 800 TPD CO 2 Capture Plant Two Trains: Absorption Columns:14.5 ft ID x high 119 ft Stripper Columns: 12.5 ft ID x 77 ft high CO 2 Use: Raw material for Na 2 CO 3
3 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, SVM CO 2 Capture Plant
4 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Process Flow Diagram
5 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, SVM CO 2 Capture Plant; Main Columns
6 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Plant Design, Troubleshooting, and Optimization using PDOEngine PDOEngine, is the HTC design and diagnostic tools to troubleshoot and optimize the operation of existing acid gas treatment plants in the chemical, petrochemical, oil, and gas industries. The PDOEngine is based on proprietary rigorous models/software and accumulative experience to perform the following activities: Producing comprehensive material, momentum and energy balances. Optimum allocation of scarce resources Sensitivity analysis Process troubleshooting, debottlenecking, and optimization Single or mixed solvents recommendation to meet the production and cleanup targets. Solvent diagnostic and recommendation for suitable reclaiming process.
7 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Rate Based Model Validation i Comparison Performance Parameters: Comparison Performance Parameters: Production capacity, solvent circulation rate, rich loading, rich solvent concentration, steam consumptions, temperatures of the main streams, flow rate of main streams, and composition of main streams
8 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, SVM, Measured and Predicted Performance, AAD% ± 6.7 odel ou utput M 1000 Parity 100 Steam supply 10 1 AAD = 6.7% Lean loading Rich loading 0.1 Off-gas temp. Producton cap Plant data 100 CO2 Purity
9 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, SVM CO 2 Capture Plant Optimization i i Parameters Effect of Solvent Concentration Effect of L/G Ratio (Solvent Circulation Rate) Effect of Flue Gas Inlet Temperature Effect of Packing Change Objectives Reduce steam consumption for current capture capacity Increase capture capacity with available resources Improve performance by minimal revamp
10 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Effect of Solvent Concentration 20 wt% (Base Case) 22 wt% 25 wt% 100% 100% 100% 96% 94% 93% 97% 95% 84% Working Capacity Circulation Rate Steam Consumption
11 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Effect of L/G Ratio (Solvent Circ. Rate) 1928 Usgpm (Base Case) 2025 USgpm 2055 USgpm 105% 107% 100% 100% 100% 95% 94% 96% 95% Working Capacity Circulation Rate Sp. Steam Consumption
12 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Effect of Flue Gas Inlet Temperature 136 F 122 F 113 F 109% 113% 100% 100% 100% 92% 88% 88% 86% Working Capacity Circulation Rate Sp. Steam Consumption
13 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Effect of Packing Change Temperature Profile (2 in Pall Ring) Temperature Profile (IMTP#40) Segme ent Temperature, o F
14 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Effect of Packing Change Segme ent Loading Profile (2 in Pall Ring) Loading Profile (IMTP#40) CO2 Loading, mol/mol
15 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Effect of Packing Change 2" Pall Ring g( (Base Case) IMTP40 at 136F IMTP40 at 113F 144% 156% 100% 100% 100% 70% 64% 79% 76% Working Capacity Circulation Rate Sp. Steam Consumption
16 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Summary of fresults Scenario Solvent Reboiler Solvent circulation steam Working consumption Capacity Increasing the solvent concentration Relaxing the solvent loading approach Reducing the flue gas temperature Changing the existing packing 7% 5% 16% 7% 5% 6% 12% 14% 13% 30% 21% 56%
17 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, Recommendations Implement the optimum operating parameters IMTP # 40 or equivalent is recommended Efficiency of Liquid Distributor/redistributor is to be investigated further Flue gas cooling below 115 F is recommended for improved plant performance
18 September 8, 2015 PCCC3, Regina, SK, Canada, September 8-11, THANK YOU For more information: Ahmed Aboudheir Victoria Ave Regina, SK, S4P 0S7, Canada
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