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Engineering decision cases

The number that changes the project.

These are simulated educational cases built around the decisions cement plants actually have to defend: process performance first, investment value second.

Do not accept the first attractive answer

A low fuel price, a high exhaust temperature or a larger fan can look like a clear opportunity. The useful question is what happens after moisture, ash, capacity, pressure loss, maintenance and lost production are counted.

How to read these cases: simulated educational scenarios. Plant names and figures are fictional training data, not claims about a real company or historical failure.

Alternative Fuels

Decision cases about RDF/SRF, moisture, NCV, ash, chlorine, kiln capacity and fuel economics.

Egyptian Plant A · RDF/SRF

The cheap RDF contract that reduced kiln production

The supplier price per tonne is lower than the current fuel cost. The contract appears profitable until the plant checks moisture, NCV, ash, chlorine and the extra fuel mass required.

Your decision: Should the contract be approved from price per tonne alone?

  • Compare delivered useful heat, not tonnes
  • Calculate moisture and NCV effects
  • Check ash, chlorine and bypass consequences
  • Include production loss, OPEX and maintenance

Regional Decision Library

Additional country-specific cases ready for review and expansion.

Saudi Plant A ·

The WHR system that generated electricity but destroyed the project return

Your decision: What should the plant do next?

    Egyptian Plant A ·

    The cheap RDF contract that reduced kiln production

    Your decision: What should the plant do next?

      Turkish Plant A ·

      The kiln expansion that was really a cooler bottleneck

      Your decision: What should the plant do next?

        Oman Plant A ·

        The WHR project that made the fan the new bottleneck

        Your decision: What should the plant do next?

          Jordan Plant A ·

          The bypass that solved chlorine and lost its payback

          Your decision: What should the plant do next?

            Yemen Plant A ·

            The damper that reduced airflow and increased the electricity bill

            Your decision: What should the plant do next?

              Saudi Plant B ·

              The fuel substitution that filled the kiln with ash

              Your decision: What should the plant do next?

                Egyptian Plant B ·

                The mill saving that increased cost per tonne

                Your decision: What should the plant do next?

                  Turkish Plant B ·

                  The kiln project delayed by a raw-mill moisture assumption

                  Your decision: What should the plant do next?

                    Oman Plant B ·

                    The alternative fuel with a perfect substitution rate and the wrong heat balance

                    Your decision: What should the plant do next?

                      Jordan Plant B ·

                      The WHR payback that existed only on a spreadsheet

                      Your decision: What should the plant do next?

                        Yemen Plant B ·

                        The capacity increase that failed the cement quality test

                        Your decision: What should the plant do next?

                          Waste Heat Recovery

                          Decision cases about recoverable heat, system limits, electricity generation and project return.

                          Saudi Plant A · WHR

                          The WHR system that generated electricity but destroyed the project return

                          A preliminary WHR proposal uses one high exhaust-temperature reading and promises a short payback. The plant has seasonal production changes and frequent kiln stops.

                          Your decision: What must be checked before approving the CAPEX?

                          • Waste-heat availability over the operating year
                          • Gas flow, dust and pressure-loss effects
                          • Electrical output, maintenance cost and production risk
                          • Payback under realistic operating hours