Design of Plant for Industrial Production of Ethylene in Kazakhstan

dc.contributor.advisorGolman, Boris
dc.contributor.advisorMentbayeva, Almagul
dc.contributor.authorTokenov, Almas
dc.contributor.authorTleubekova, Akkerbez
dc.contributor.authorTuleshov, Bektaiyr
dc.contributor.authorAgassultanov, Rakhat
dc.contributor.authorLukmanov, Islam
dc.date.accessioned2026-06-15T10:11:31Z
dc.date.issued2026-05
dc.description.abstractEthylene is a fundamental petrochemical building block, yet no dedicated production facility currently operates in Kazakhstan despite abundant local ethane resources. This capstone project presents the complete front-end engineering design of a 300,000 metric tonnes per year polymer-grade ethylene plant to be located in the Atyrau region, utilizing ethane steam cracking as the production route. The process design was developed through rigorous Aspen Plus V14 simulation, employing the RK-SOAVE equation of state to model the cracking furnace, quench system, three-stage cracked-gas compression train, cryogenic fractionation sequence (demethanizer, depropanizer, deethanizer), acetylene hydrogenation unit, and C2 splitter for ethylene-ethane separation. Key equipment including the cracking furnace (77 tubular reactors, HP40-Nb alloy), shell-and-tube heat exchangers, distillation columns (demethanizer with 84 actual stages, C2 splitter with 63 trays), and two-stage adiabatic packed-bed hydrogenation reactors (Pd-Ag/Al₂O₃ catalyst) were sized using Fenske-Underwood-Gilliland methods, Ergun pressure drop correlations, and LHHW kinetics. Material and energy balances were closed at 39,000 kg/h ethane feed, producing 35,941 kg/h of 99.95 mol% ethylene. The plant layout was designed for the SEZ "National Industrial Petrochemical Technopark" near Atyrau, incorporating API 752 separation distances, NFPA 30 requirements, and a six-node HAZOP analysis identifying two SIL-2 safety functions. Economic evaluation at 2025 price levels gave a total fixed capital investment of USD 502 million, annual operating costs of USD 139 million, base-year revenue of USD 287 million, net present value of USD 347 million, internal rate of return of 34.6%, and a payback period of 4.2 years from construction start. The design demonstrates technical feasibility and commercial viability for ethylene production in Kazakhstan, leveraging local feedstock, existing infrastructure, and special economic zone incentives.
dc.identifier.citationAgassultanov, R., Lukmanov, I., Tuleshov, B., Tokenov, A. & Tleubekova, A. (2026). Design of plant for industrial production of ethylene in Kazakhstan. Nazarbayev University School of Engineering and Digital Sciences.
dc.identifier.urihttps://nur.nu.edu.kz/handle/123456789/19234
dc.language.isoen
dc.publisherNazarbayev University School of Engineering and Digital Sciences
dc.rightsAttribution-NonCommercial 3.0 United Statesen
dc.rights.urihttp://creativecommons.org/licenses/by-nc/3.0/us/
dc.subjectEthylene Production
dc.subjectEthane Steam Cracking
dc.subjectProcess Simulation
dc.subjectEquipment Sizing
dc.subjectTechno-Economic Analysis
dc.subjectKazakhstan Petrochemicals
dc.titleDesign of Plant for Industrial Production of Ethylene in Kazakhstan
dc.typeBachelor's Capstone project

Files

Original bundle

Now showing 1 - 1 of 1
Loading...
Thumbnail Image
Name:
Design of Plant for Industrial Production of Ethylene in Kazakhstan
Size:
11.5 MB
Format:
Adobe Portable Document Format
Description:
Bachelor`s Capstone Project