Facility;Client;Development Stage;Year;Note

Pentane-Hexane Cut Isomerasation Unit ПГИ-434 at OJSC "Gaspromneftechim Salavat"; OJSC "Salavatnefte-khimremstroy"; Design and Detailed Design Documentation; 2012-2015; Licensor – Axens. FAU “RF Glavgosexpertisa” favourable conclusion. Commissioned in 2017 Low-temperature Isomerization Complex with NHT, Hydrogenation and Deisohexanization Sections PGI-DIH/280-NK at Novokuibyshevsk Refinery ; OJSC "Samaraneftekhimproect"; Detailed Design Documentation; 2010-2014; Licensor – Axens. FAU “RF Glavgosexpertisa” favourable conclusion. Commissioned in February 2015 Isomerization Unit with DHT, Hydrogenation and Deisohexanization Sections PGI-DIH/280-K at Kuibyshev Refinery; OJSC "Samaraneftekhimproect"; Detailed Design Documentation; 2009-2012; Licensor – Axens. FAU “RF Glavgosexpertisa” favourable conclusion. Commissioned in September 2014 С5-С6 Cut Isomerization Unit at Novokuibyshevsk Refinery ; OJSC "Samaraneftekhimproect"; Technical assistance during Basic Design Acceptance; 2009; Licensor – Axens Isomerization Unit with DHT, Hydrogenation and Deisohexanization Sections PGI-DIH/280, Syzran Refinery; Syzran Refinery, OC ROSNEFT; Detailed Design; 2006-2009; Licensor – Axens. FAU “RF Glavgosexpertisa” favourable conclusion. Commissioned in 2011 IBP-85°С Cut Isomerization Unit with feed-preparation and Deisopentanization Sections of capacity 80,000 tons/year; Khersonneftepererabotka Company, Ukraine; Detailed Design; 2004; Submitted for approval in 2006 n-butane Isomerization Unit of 50,000 tons/year ; AD LUKOIL Neftochim Bourgas, Bulgaria; Detailed Design Documentation; 2004-2007; Licensor – Axens. Commissioned in 2008 Isomerization Unit PI-DIH/120 of capacity 120,000 tons/year; LUKOIL-Odessa Refinery, Ukraine; Detailed Design; 2003; Licensor – UOP. Commissioned in August 2004 Isomerization and Oligomerization Units; LINOS Company; Feasibility Study; 2002; Addition of 170,000 tpy to Catalytic Reforming Unit; Petrotel-LUKOIL Refinery, Romania; Detailed Design ; 2000-2001; Licensor – UOP. Commissioned in 2001 Addition of 213,000 tpy Isomerization Unit to L-35-11/300 Unit ; Moscow Refinery, Korimos Company, Moscow; Detailed Design; 2000-2001; Licensor – Süd-Chemie. Construction of the unit has been suspended PI-200 Unit. Stack. Unit Heaters. Technological part of the Process Operating Regulations for Hydrotreating Section Design; LUKOIL-Permnefteorgsyntez Company; Detailed Design; 1996; PI-200 Unit. Hydrotreating Reactor; LUKOIL-Permnefteorgsyntez Company; Detailed Design; 1994; Provision of Services for Ordering Equipment for ПИ-200 Isomerization Unit and Work Coordination on Use of Existing Parex-2M Unit Equipment in PI-200 Unit; Permnefteorgsyntez Company, Lengiproneftekhim Company, St. Petersburg; Completing a set equipment for the unit ; 1993-1994