Catalytic conversion of vacuum gas oil and compatible heavy feeds into gasoline, LPG, light cycle oil and gas.
Feed injection, riser cracking, catalyst separation, regeneration, main fractionation and gas concentration. The operating sequence, recycle paths, start-up/shutdown cases and normal/turndown behavior are defined before equipment finalization.
Riser/reactor, regenerator, cyclones, main fractionator, wet-gas compressor, absorbers and debutanizer. Materials, design margins, maintainability, isolation, access, lifting and spare philosophy are coordinated with the approved operating cases.
Feed assay/composition, design capacity, operating pressure and temperature, product specifications, turndown, utilities, battery limits and site ambient conditions.
Licensor integration, yield balance, catalyst/coke balance, equipment interfaces, PFD/P&ID and safeguards. The package also includes line/equipment lists, relief and utility summaries, layouts or 3D interfaces, vendor-document requirements, inspection plans and commissioning inputs as applicable.
DCS regulatory control, critical interlocks, relief and depressuring, gas/fire detection, hazardous-area classification, HAZOP actions and applicable SIS/ESD functions.
High-conversion refineries targeting gasoline, LPG/propylene and distillate blendstocks. Capacity, product quality, consumption and emissions commitments are confirmed only after the representative feed and project Design Basis are approved.
Licensor standards, API, ASME, refractory, emissions and high-temperature design requirements. The contractual code basis is selected by destination and client specification. ASME/API/TEMA, EN/DIN and GOST/EAC requirements are not mixed without an approved code-equivalency and authority review.
Licensor standards, API, ASME, refractory, emissions and high-temperature design requirements.