Saint-Petersburg:
Rostov-on-Don:
Catalytic Reforming Units with NHT sections:
Facility;Client;Development Stage;Year;Note
Modernization of motor oil production in order to provide Euro 4 and 5 quality at Astrakhan Gas Processing Plant consisting of: - Catalytic Reforming Unit У-1.734, - Benzol Cut Recovery Block; LLC "SRDI OG Peton", Ufa; Detailed Design Documentation; 2014;
Revamping of Hydrotreatment Section at Catalytic Reforming Unit 95 to increase its capacity to 575,000 tpy at OJSC "Khabarovsk Oil Refinery"; OJSC "Khabarovsk Oil Refinery"; Design Documentation, Detailed Design Documentation ; 2014;
Revamping of heater section of unit LG-35-11/300-95 at JSC "LUKOIL-Ukhtaneftepererabotka"; JSC "LUKOIL-Ukhtaneftepererabotka"; Detailed Design Documentation; 2012; Heater section is comissioned in September 2012
Revamping of Unit L-35/11-1000 at Kuibyshev Refinery aimed to operate at reduced pressure in reformer section; OJSC "Samaraneftekhimproect"; Design Documentation Detailed Design Documentation; 2010-2015; FAU “RF Glavgosexpertisa”s favourable conclusion
Piping of CRU plate heat exchanger in refinery complex LK-6U in LLC “Petro-Kazakhstan Oil Products”; PetroKazakhstan Oil Products, Shymkent, Republic of Kazakhstan; Detailed Design Documentation; 2010; Mounted in February 2011
Catalytic Reformer Unit with CCR, capacity 748,000 tpy; OJSC “NPK – Galychina”, Ukraine; Project Documentation, Detailed Design Documentation; 2008; Part of documentation was developed, Financing is suspended
Revamping of Catalytic Reformer Unit LG-35-11/300 to increase capacity to 450,000 tpy at Khabarovsk Refinery; Khabarovsk Refinery, OC Alliance; Detailed Design Documentation; 2007-2010; Licensor – Criterion. 1st phase – brought to capacity 350 000 in 3rd quarter 2010 t/y
Revamping of Unit LCh-35/11-600 at Syzran Refinery; Syzran Refinery, OC ROSNEFT; Detailed Design; 2007-2009; Licensor – Axens. FAU “RF Glavgosexpertisa”s favourable conclusion. Commissioned in 2011
Installation and connections of the reciprocating compressor for Unit LG-35-11/300 at LUKOIL-Odessa Refinery; LUKOIL-Odessa Refinery, Ukraine; Detailed Design Documentation; 2007;
Upgrading of section 200 “Catalytic Reforming” of Unit LK-6U and construction of “Recontact” Section; PetroKazakhstan Oil Products, Shymkent, Republic of Kazakhstan; Detailed Design Documentation; 2004; Licensor – UOP. Detailed Design Documentation on the 1st stage was handed over to the Refinery. Financing was suspended
Automated process control system of Units LG-35-УВПБ for LUKOIL-Odessa Refinery; LUKOIL-Odessa Refinery, Ukraine; Detailed Design; 2004-2005; Installed in 2005
Upgrading of Unit LG-35-11/300-95 to increase capacity to 450,000 tons/year (based on feed flow rate); Khabarovsk Refinery, OC Alliance; Basic Design (using Criterion catalyst); 2003; Licensor – Criterion
Installation of feed heat- exchanger of PAKINOX type in Reforming Section of LG-35-11/300-95 Unit; LUKOIL-Odessa Refinery, Ukraine; Detailed Design Documentation; 2003; Installation was completed in February 2004
Upgrading of Unit L-35-11/600. Recommendations on operation of heaters P-201 and P-202 for capacity Qmin =250 000 tons/year and Qmax=350 000 tons/year; Khersonneftepererabotka Company, Ukraine; Recommendations; 2003;
Upgrading of Unit L-35-11/600. Recommendations on operation of Unit L-35-11/600 at pressure 18 kgf/cm2 (gage) in the last reactor of Catalytic Reforming section for capacity Qmin =250 000 tons/year and Qmax=350 000 tons/year; Khersonneftepererabotka Company, Ukraine; Recommendations; 2003;
Revamping of L-35-8/300Б Unit to increase its capacity to 400,000 tpy; LUKOIL-Volgogradneftepererabotka Company; Detailed Design; 2002; Licensor – UOP. Commissioned in 2003
Upgrading of Unit LG-35-11/600. Calculation of sulfur trap pipe system; Khersonneftepererabotka Company, Ukraine; Calculations and detailed design documentation; 2002; Licensor – VNIINeftechim, St. Petersburg. Commissioned in 2003
Hydrogen-Rich Gas Drying Section and Hydrotreating and Reforming Catalyst Regeneration Section of VR-650 Unit; LUKOIL-Western Siberia, Uraineftegaz Refinery; Detailed Design Documentation; 2002; Installed in 2003
Protection of Catalytic Reforming Equipment against Organic Chloride Corrosion; Syzran Refinery,OC Rosneft; Design; 2002; Installed in 2003
Hydrotreating Sections of Catalytic Reforming Units at Syzran Refinery; Syzran Refinery, OC Rosneft; Recommendations regarding equipment protection against corrosion and salt formation; 2002;
Upgrading of LG-35-11/300 Catalytic Reforming Unit to increase its capacity to 380,000 tpy for LUKOIL-Ukhtaneftepererabotka Company; LUKOIL-Rostovneftekhimproekt Company; Detailed Design; 2002-2004; Licensor – UOP. Commissioned in 2004
Revamping of LG-35-11/300 Catalytic Reforming Unit at LUKOIL-Ukhtanefte-pererabotka Company; UOP, Great Britain; Feasibility Study; 2001;
Revamping of LG-35-11/300 Catalytic Reforming Unit at LUKOIL-Odessa Refinery; LUKOIL-Odessa Refinery, Ukraine; Process Calculations and Assignment for supply of Packinox Heat-Exchanger; 2001;
1,000,000 tpy Catalytic Reforming Unit with Afterfractionating Section (PR- 22-35-11/1000) for LUKOIL-Volgogradneftepererabotka Company; LUKOIL-Rostovneftekhimproekt Company; Detailed Design; 2000-2006; Licensor– UOP. Commissioned in 2006
Upgrading of L-35-11/300 Unit; Saratov Refinery, OC SIDANKO; Justification of Investments; 2001;
Revamping of the L-35-8/300-B Unit; LUKOIL-Permnefteorgsyntez; Feasibility Study; 2000;
Revamping of CR-1 Catalytic Reforming Unit, AD LUKOIL-Neftochim Bourgas, Bulgaria; LUKOIL-Rostovneftekhimproekt Company; Process Part of Business Plan; 2000;
Revamping of L-35-8/З00B Aromatic Hydrocarbons Unit for LUKOIL-Volgogradneftepererabotka Company; UOP, Great Britain; Feasibility Study; 1999;
Replacement of Separator in L-35-11/300 Unit; KINEF, Kirishi, Leningrad Region; Detailed Design; 1999; Installed in 1999
Upgrading of LCh-35-11/600 Unit; KINEF Company, Kirishi, Leningrad Region; Technical and Commercial Proposal; 1999;
500,000 tpy Catalytic Reforming Unit with NHT Section; Komsomolsk Refinery-Rosneft, Komsomolsk-on-Amur; Justification of Investments; 1999;
Control system upgrading in LCh–35-11/1000 Unit; KINEF Company, Kirishi, Leningrad Region; Technical and Commercial Proposal; 1999;
Regeneration Gas Treatment Section in L -35-11/300 Unit; Tuapse Refinery, OC ROSNEFT; Detailed Design Documentation; 1998; Сommissioned in 1998
Replacement of Reactor Effluent Separator of NHT Section in L-35-11/300 Unit; KINEF Company, Kirishi, Leningrad Region; Technical and Commercial Proposal; 1998;
Gas Recovery Section of Reforming Unit with capacity of 20,000 tpy; LUKOIL-Uraineftegaz Companyi; Detailed Design; 1997; Commissioned in 1998
Revamping of L-35-11/300 Unit to increase its capacity to 400,000 tpy; Tuapse Refinery, OC ROSNEFT; Technical and Commercial Proposal; 1997;
Revamping of LCh-35-11/1000 Catalytic Reforming Unit for Seidinsky Refinery (Chardzhou); GRIMMA, West Germany, FRG; Technical and Commercial Proposal; 1997;
Replacement of L-35-11/300 NHT Reactor; Moscow Refinery; Detailed Design Documentation; 1996; Installed in 1997
Revamping of Reactor and Heater section of L-35-11/300 Unit; Moscow Refinery; Detailed Design Documentation; 1996; Licensor – UOP. Commissioned in 1997
Revamping of L-35-11/300 Unit to increase its capacity to 450,000 tons/year; Moscow Refinery; Technical and Commercial Proposal; 1996;
Addition of Pre-contactor and Revamping of Heater Section of L-35-11/300 Unit; Tuapse Refinery,OC ROSNEFT; Check Calculations and Detailed Design Documentation; 1996; Revamped in 1998
1,000,000 tpy Naphtha Fractions Mixture Catalytic Reforming Unit; Turkmenbashi Refinery, Turkmenia; Technical and Commercial Proposal; 1996
Facility;Client;Development Stage;Year;Note
Modernization of motor oil production in order to provide Euro 4 and 5 quality at Astrakhan Gas Processing Plant consisting of: - Catalytic Reforming Unit У-1.734, - Benzol Cut Recovery Block; LLC "SRDI OG Peton", Ufa; Detailed Design Documentation; 2014;
Revamping of Hydrotreatment Section at Catalytic Reforming Unit 95 to increase its capacity to 575,000 tpy at OJSC "Khabarovsk Oil Refinery"; OJSC "Khabarovsk Oil Refinery"; Design Documentation, Detailed Design Documentation ; 2014;
Revamping of heater section of unit LG-35-11/300-95 at JSC "LUKOIL-Ukhtaneftepererabotka"; JSC "LUKOIL-Ukhtaneftepererabotka"; Detailed Design Documentation; 2012; Heater section is comissioned in September 2012
Revamping of Unit L-35/11-1000 at Kuibyshev Refinery aimed to operate at reduced pressure in reformer section; OJSC "Samaraneftekhimproect"; Design Documentation Detailed Design Documentation; 2010-2015; FAU “RF Glavgosexpertisa”s favourable conclusion
Piping of CRU plate heat exchanger in refinery complex LK-6U in LLC “Petro-Kazakhstan Oil Products”; PetroKazakhstan Oil Products, Shymkent, Republic of Kazakhstan; Detailed Design Documentation; 2010; Mounted in February 2011
Catalytic Reformer Unit with CCR, capacity 748,000 tpy; OJSC “NPK – Galychina”, Ukraine; Project Documentation, Detailed Design Documentation; 2008; Part of documentation was developed, Financing is suspended
Revamping of Catalytic Reformer Unit LG-35-11/300 to increase capacity to 450,000 tpy at Khabarovsk Refinery; Khabarovsk Refinery, OC Alliance; Detailed Design Documentation; 2007-2010; Licensor – Criterion. 1st phase – brought to capacity 350 000 in 3rd quarter 2010 t/y
Revamping of Unit LCh-35/11-600 at Syzran Refinery; Syzran Refinery, OC ROSNEFT; Detailed Design; 2007-2009; Licensor – Axens. FAU “RF Glavgosexpertisa”s favourable conclusion. Commissioned in 2011
Installation and connections of the reciprocating compressor for Unit LG-35-11/300 at LUKOIL-Odessa Refinery; LUKOIL-Odessa Refinery, Ukraine; Detailed Design Documentation; 2007;
Upgrading of section 200 “Catalytic Reforming” of Unit LK-6U and construction of “Recontact” Section; PetroKazakhstan Oil Products, Shymkent, Republic of Kazakhstan; Detailed Design Documentation; 2004; Licensor – UOP. Detailed Design Documentation on the 1st stage was handed over to the Refinery. Financing was suspended
Automated process control system of Units LG-35-УВПБ for LUKOIL-Odessa Refinery; LUKOIL-Odessa Refinery, Ukraine; Detailed Design; 2004-2005; Installed in 2005
Upgrading of Unit LG-35-11/300-95 to increase capacity to 450,000 tons/year (based on feed flow rate); Khabarovsk Refinery, OC Alliance; Basic Design (using Criterion catalyst); 2003; Licensor – Criterion
Installation of feed heat- exchanger of PAKINOX type in Reforming Section of LG-35-11/300-95 Unit; LUKOIL-Odessa Refinery, Ukraine; Detailed Design Documentation; 2003; Installation was completed in February 2004
Upgrading of Unit L-35-11/600. Recommendations on operation of heaters P-201 and P-202 for capacity Qmin =250 000 tons/year and Qmax=350 000 tons/year; Khersonneftepererabotka Company, Ukraine; Recommendations; 2003;
Upgrading of Unit L-35-11/600. Recommendations on operation of Unit L-35-11/600 at pressure 18 kgf/cm2 (gage) in the last reactor of Catalytic Reforming section for capacity Qmin =250 000 tons/year and Qmax=350 000 tons/year; Khersonneftepererabotka Company, Ukraine; Recommendations; 2003;
Revamping of L-35-8/300Б Unit to increase its capacity to 400,000 tpy; LUKOIL-Volgogradneftepererabotka Company; Detailed Design; 2002; Licensor – UOP. Commissioned in 2003
Upgrading of Unit LG-35-11/600. Calculation of sulfur trap pipe system; Khersonneftepererabotka Company, Ukraine; Calculations and detailed design documentation; 2002; Licensor – VNIINeftechim, St. Petersburg. Commissioned in 2003
Hydrogen-Rich Gas Drying Section and Hydrotreating and Reforming Catalyst Regeneration Section of VR-650 Unit; LUKOIL-Western Siberia, Uraineftegaz Refinery; Detailed Design Documentation; 2002; Installed in 2003
Protection of Catalytic Reforming Equipment against Organic Chloride Corrosion; Syzran Refinery,OC Rosneft; Design; 2002; Installed in 2003
Hydrotreating Sections of Catalytic Reforming Units at Syzran Refinery; Syzran Refinery, OC Rosneft; Recommendations regarding equipment protection against corrosion and salt formation; 2002;
Upgrading of LG-35-11/300 Catalytic Reforming Unit to increase its capacity to 380,000 tpy for LUKOIL-Ukhtaneftepererabotka Company; LUKOIL-Rostovneftekhimproekt Company; Detailed Design; 2002-2004; Licensor – UOP. Commissioned in 2004
Revamping of LG-35-11/300 Catalytic Reforming Unit at LUKOIL-Ukhtanefte-pererabotka Company; UOP, Great Britain; Feasibility Study; 2001;
Revamping of LG-35-11/300 Catalytic Reforming Unit at LUKOIL-Odessa Refinery; LUKOIL-Odessa Refinery, Ukraine; Process Calculations and Assignment for supply of Packinox Heat-Exchanger; 2001;
1,000,000 tpy Catalytic Reforming Unit with Afterfractionating Section (PR- 22-35-11/1000) for LUKOIL-Volgogradneftepererabotka Company; LUKOIL-Rostovneftekhimproekt Company; Detailed Design; 2000-2006; Licensor– UOP. Commissioned in 2006
Upgrading of L-35-11/300 Unit; Saratov Refinery, OC SIDANKO; Justification of Investments; 2001;
Revamping of the L-35-8/300-B Unit; LUKOIL-Permnefteorgsyntez; Feasibility Study; 2000;
Revamping of CR-1 Catalytic Reforming Unit, AD LUKOIL-Neftochim Bourgas, Bulgaria; LUKOIL-Rostovneftekhimproekt Company; Process Part of Business Plan; 2000;
Revamping of L-35-8/З00B Aromatic Hydrocarbons Unit for LUKOIL-Volgogradneftepererabotka Company; UOP, Great Britain; Feasibility Study; 1999;
Replacement of Separator in L-35-11/300 Unit; KINEF, Kirishi, Leningrad Region; Detailed Design; 1999; Installed in 1999
Upgrading of LCh-35-11/600 Unit; KINEF Company, Kirishi, Leningrad Region; Technical and Commercial Proposal; 1999;
500,000 tpy Catalytic Reforming Unit with NHT Section; Komsomolsk Refinery-Rosneft, Komsomolsk-on-Amur; Justification of Investments; 1999;
Control system upgrading in LCh–35-11/1000 Unit; KINEF Company, Kirishi, Leningrad Region; Technical and Commercial Proposal; 1999;
Regeneration Gas Treatment Section in L -35-11/300 Unit; Tuapse Refinery, OC ROSNEFT; Detailed Design Documentation; 1998; Сommissioned in 1998
Replacement of Reactor Effluent Separator of NHT Section in L-35-11/300 Unit; KINEF Company, Kirishi, Leningrad Region; Technical and Commercial Proposal; 1998;
Gas Recovery Section of Reforming Unit with capacity of 20,000 tpy; LUKOIL-Uraineftegaz Companyi; Detailed Design; 1997; Commissioned in 1998
Revamping of L-35-11/300 Unit to increase its capacity to 400,000 tpy; Tuapse Refinery, OC ROSNEFT; Technical and Commercial Proposal; 1997;
Revamping of LCh-35-11/1000 Catalytic Reforming Unit for Seidinsky Refinery (Chardzhou); GRIMMA, West Germany, FRG; Technical and Commercial Proposal; 1997;
Replacement of L-35-11/300 NHT Reactor; Moscow Refinery; Detailed Design Documentation; 1996; Installed in 1997
Revamping of Reactor and Heater section of L-35-11/300 Unit; Moscow Refinery; Detailed Design Documentation; 1996; Licensor – UOP. Commissioned in 1997
Revamping of L-35-11/300 Unit to increase its capacity to 450,000 tons/year; Moscow Refinery; Technical and Commercial Proposal; 1996;
Addition of Pre-contactor and Revamping of Heater Section of L-35-11/300 Unit; Tuapse Refinery,OC ROSNEFT; Check Calculations and Detailed Design Documentation; 1996; Revamped in 1998
1,000,000 tpy Naphtha Fractions Mixture Catalytic Reforming Unit; Turkmenbashi Refinery, Turkmenia; Technical and Commercial Proposal; 1996
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6, lit.A, Birzhevoy pereulok,
Saint-Petersburg, Russia, 199004
+7 (812) 244-32-50
Saint-Petersburg, Russia, 199004
+7 (812) 244-32-50