PROCESS & OPERATING PHILOSOPHY
Feed hydrotreating, catalytic cracking, high-pressure separation, recycle gas and product fractionation. The operating sequence, recycle paths, start-up/shutdown cases and normal/turndown behavior are defined before equipment finalization.
MAIN EQUIPMENT & PACKAGE LIMITS
Reactors, charge heater, high-pressure exchangers/separators, recycle compressor and fractionator. Materials, design margins, maintainability, isolation, access, lifting and spare philosophy are coordinated with the approved operating cases.
CRITICAL DESIGN INPUTS
Feed assay/composition, design capacity, operating pressure and temperature, product specifications, turndown, utilities, battery limits and site ambient conditions.
ENGINEERING DELIVERABLES
Licensor/kinetic basis, hydrogen balance, high-pressure design, safeguards, PFD/P&ID and performance protocol. 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.
AUTOMATION, SAFETY & HSE
DCS regulatory control, critical interlocks, relief and depressuring, gas/fire detection, hazardous-area classification, HAZOP actions and applicable SIS/ESD functions.
APPLICATIONS & PERFORMANCE BASIS
Clean-fuels refineries requiring high middle-distillate yield and flexible conversion. Capacity, product quality, consumption and emissions commitments are confirmed only after the representative feed and project Design Basis are approved.
CODES, STANDARDS & QUALITY BASIS
API 934, ASME, NACE, licensor and high-pressure hydrogen-service 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.
CONTRACTUAL CODE BASISAPI 934, ASME, NACE, licensor and high-pressure hydrogen-service requirements.