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Analysis and design

Energy, economics and safety

Three ways to judge a solved design: how little energy it could use, what it would cost and earn, and what could go wrong. Each environment reads the flowsheet you just ran.

Energy: pinch analysis

  • Every heating and cooling duty — heaters, coolers, condensers, reboilers, reactors — becomes a hot or cold stream, listed under Thermal streams.
  • Set the minimum approach temperature, ΔTmin. LensaSim gives the hot and cold utility targets, the pinch temperature, and how far today's design is from them.
  • The composite curves and grand composite curve show where heat can be recovered; Heat-integration opportunities points to recovery between the process's own hot and cold services.
  • Utilities & carbon footprint gives the energy the utilities supply in a year and the CO₂ it emits — today and at the target — so the saving is in tonnes as well as gigajoules.

Move ΔTmin and watch the targets change: smaller saves energy and costs exchanger area.

Economics (Pro)

  • Sizing & CAPEX — each block sized from its solved duty, flow or volume and costed by module costing on a chemical-engineering cost index basis. Untick a block to leave it out; override a size, the material or a quote.
  • OPEX — raw materials, utilities, labour and the cost of manufacture.
  • Profitability — NPV, IRR, payback, the cash-flow table and a one-way sensitivity.
  • Assumptions — the cost index, utility prices and the finance basis, all editable; set feed and product prices to get revenue.
  • The TEA report prints all of it. It is a study-class estimate: good for screening and comparing options, while an investment decision needs vendor quotations.

Safety

  • Chemical hazards — each component's flammability limits, flash point, autoignition temperature, toxic level of concern and NFPA ratings.
  • Stream hazards — which streams are inside their flammable range, above autoignition, or highly toxic, and the flammable inventory.
  • Relief sizing — relief loads for the common scenarios and the orifice area each needs, by the API 521 and API 520 methods.
  • HAZOP worksheet — guide words applied to your flowsheet, with causes, consequences and safeguards to complete.

These are screening tools: check every hazard against the Safety Data Sheet, and treat relief numbers as the starting point for a detailed design.

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