IMPLEMENTATIONS
DMC-1 process (Tengiz crude demercaptanization plant)
Kazakhstan, J.V. «Tengizchevroil»
In operation since 1995(1 line), 1996 (2 line)
Capacity – 2 x 4 MMt/yr (2 x 80 000 bbl/day),
after modification in 1999 the capacity is 2 x 6.5 MM t/yr (2 x 130 000 bbl/day). Catalyst – IVKAZ
Mercaptan sulfur content (methyl- and ethyl mercaptans):
before treatment – 0.026÷0.03 % mass (260÷300 ppm)
after treatment – 0.002 % mass ( 20 ppm)
The design was developed by «Bechtel Co.», England
The plant was equipped and mounted by «Brown and Root Co.»
DMD-2 process (n-Pentane demercaptanization plant)
Russia, Novokuibyshevsk PCC
In operation since 1974
Capacity – 120 000 t/yr (3 800 bbl/day)
DMD-2 process (demercaptanization plant for C2-C6 fraction)
Russia, J.S. «Salavatnefteorgsintez»
In operation since 1975
Capacity – 400 000 t/yr (12 700 bbl/day)
DMD-2 process (demercaptanization plant for butane-butylene fraction)
Russia, J.S. «Salavatnefteorgsintez»
In operation since 1976
Capacity – 600 000 t/yr (19 000 bbl/day)
DMD-2 process (demercaptanization plant for butane-butylene fraction)
Russia, Kuibyshev Oil Refinery
In operation since 1977
Capacity – 130 000 t/yr (4 000 bbl/day)
DMD-2 ODORANT process
(gas condensate demercaptanization and odorant production)
Russia, J.S. «Orenburg Gazprom»
In operation since 1983
Capacity:
for condensate – 600 000 t/yr (12 000 bbl/day)
for odorant production – 3 000 t/yr
DMD-2 process
(demercaptanization of butane-butylene and pentane-amylene fractions)
Russia, Ryazan Oil Refinery
In operation since 1985
Capacity – 125 000 t/yr (4 000 bbl/day)
DMD-2 process (demercaptanization plant for butane- butylene fraction)
Lithuania, Mazheikai Oil Refinery
In operation since 1990
Capacity – 220 000 t/yr (7 000 bbl/day)
Serox-W process (plant for sulfur-alkaline waste water treatment)
Lithuania, Mazheikai Oil Refinery
In operation since 1990
Capacity – 25 m3/hr
Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Moscow Oil Refinery
In operation since 1990
Capacity – 30 m3/hr
DMD-2 process (demercaptanization plant for butane-butylene fraction)
Russia, Ufa Oil Refinery
In operation since 1991
Capacity – 220 000 t/yr (7 000 bbl/day)
Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Ryazan Oil Refinery
In operation since 1991
Capacity – 20 m3/hr
Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Pavlodar Oil Refinery
In operation since 1991
Capacity – 25 m3/hr
DMD-2 process (demercaptanization plant for butane- butylene fraction)
Russia, Moscow Oil Refinery
In operation since 1992
Capacity – 220 000 t/yr (7 000 bbl/day)
DMD-2 process (demercaptanization plant for liquefied gases)
Russia, J.S. «Astrakhan Gasprom»
In operation since 1992
Capacity – 400 000 t/yr (13 000 bbl/day)
Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Omsk Oil Refinery
In operation since 1992
Capacity – 20 m3/hr
Serox-W process (plant for sulfur -alkaline waste water treatment)
Bulgaria, Burgas Oil Refinery
In operation since 1994
Capacity – 5 m3/hr
Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Kuibyshev oil refinery
In operation since 1996
Capacity – 6 m3/hr
Complex for demercaptanization of light petroleum fractions
Russia, Samara Oil Refinery
In operation since 1996
DMD-2 unit of C3-C4 fraction treatment for 200 000 t/yr (6 400 bbl/day)
DMD-2 unit of C5 fraction treatment for 110 000 t/yr (3 400 bbl/day)
DMD-3 unit of C6+ fraction treatment for 310 000 t/ yr (9 000 bbl/day)
Serox-W unit of sulfur-alkaline waste water treatment for 6 m3/hr
DMD-4 process
(plant for iso-pentane fraction treatment for dimethyl sulfide)
Russia, Sterlitamak, J.S. «Cauchuk»
In operation since 1996
Capacity – 25 000 t/yr (800 bbl/day)
Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Yaroslavl oil refinery
In operation since 1999
Capacity – 20 m3/hr
DMC-3 process (demercaptanization plant for gas condensate)
Russia, Orenburg, J.S. «YUPK»
In operation since 2000
Capacity – 2 MM t/yr (40 000 bbl/day)
DMD-1 process (demercaptanization plant for kerosene)
Russia, Kuibyshev oil refinery
In operation since 2000
Capacity – 310 000 t/yr (6 500 bbl/day)
DMD-2 process (demercaptanization plant for C2-C6 fraction)
Russia, Perm Oil Refinery
In operation since 2000
Capacity – 300 000 t/yr (9 500 bbl/day)
DMD-4 process
(plant for iso-pentane fraction treatment for dimethyl sulfide)
Russia, J.S. «Novokuibychevskaya khimicheskaya kompaniya»
In operation since 2000
Capacity – 40 000 t/yr (1 300 bbl/day)
DMC-1M process (demercaptanization plant for crude oil )
Kazakhstan, «CNPC-Aktobemunaigaz»
In operation since 2001
Capacity – 2.5 MM t/yr (50 000 bbl/day)
DMD-2 process (demercaptanization plant for C2-C6 fraction )
Russia, J.S. «Novokuibyshevsk Petrochemical Company»
In operation since 2002
Capacity – 150 000 t/yr (4 700 bbl/day)
DMC-3 process (demercaptanization plant for gas condensate)
Lithuania, J.S. «Mazheiku Nafta»
In operation since 2002
Capacity – 700 000 t/yr (14 000 bbl/day)
DMD-1 process (demercaptanization plant for kerosene)
Russia, Ukhta Oil Refinery
In operation since 2002
Capacity – 50 000 t/yr (1 000 bbl/day)
DMC-1M process (demercaptanization plant for crude oil)
Kazakhstan, J.S. «Kazakhoil Aktobe»
In operation since 2002
Capacity – 2.5 MM t/yr (50 000 bbl/day)
DMC-2 process (demercaptanization plant for condensate)
Latvia, J.S. «Stena» (crude oil tank farm)
In operation since 2003
Capacity – 150 m3/hr (22 500 bbl/day)
DMD-2 process (demercaptanization plant for butane- butylene fraction)
Russia, Omsk oil refinery
In operation since 2003
Capacity – 150 000 t/yr (4 700 bbl/day)
DMD-2 process (demercaptanization plant for propane- butane fraction)
Russia, Orenburg gas refinery
In operation since 2003
Capacity – 550 000 t/yr (17 500 bbl/day)
DMC-2 process (demercaptanization plant for gas condensate)
Russia, Taganrog, J.S. «Neklinovsknefteproduct» (crude oil tank farm)
In operation since 2004
Capacity – 150 m3/hr (22 500 bbl/day)
DMC-3 process (demercaptanization plant for crude oil )
Kazakhstan, J.S. «Kazakhoil Aktobe»
In operation since 2004
Capacity – 3 300 t/day (24 000 bbl/day)
DMD-3 + DMD-2 processes
(pilot demercaptanization plant for gasoline and liquefied gases)
Iran, Tehran, Iranian Research Institute of Petroleum Industry «RIPI»
In operation since 2002
Capacity – 100 liters/hr (15 bbl/day)
DMC-1MA process (plant for heavy oil treatment for hydrogen sulfide and mercaptans)
Tatarstan, J.S. «Tatneft», NGDU «Nurlatneft»
In operation since 2005
Capacity – 4 900 t/day (34 000 bbl/day)
Serox-W process (plant for sulfur-alkaline waste water treatment)
Belorussia, Novopolotsk, J.S. «NAFTAN»
In operation since 2005
Capacity – 0.25 m3/hr
DMC-1 process (demercaptanization plant for oil)
Kazakhstan, J.S. «KDO»
In operation since 2006
Capacity – 200 000 t/yr (4 500 bbl/day)
DMD-2 process (demercaptanization plant for IBP-70°C fraction of catalytic cracking)
Russia, Nizhnekamsk, Gasoline Plant of J.S. «TAIF-NK»
In operation since 2007
Capacity – 300 000 t/yr (9 000 bbl/day)
DMD-2 process (demercaptanization plant for butane fraction)
Bulgary, Burgas, «Lukoil Neftochim Burgas AD»
In operation since 2007
Capacity – 100 000 t/yr (3 000 bbl/day)
Process for associated oil gas treating for hydrogen sulfide
Russia, Almetyevsk, J.S.”Troitskneft”
In operation since 2007
Capacity – 3 MM m3/year
Demercaptanization complex for naphtha and liquefied gases
Iran, Kharg island, KHARG Petrochemical Co.
DMD-2 unit of propane treatment for 165 000 t/yr (6 300 bbl/day)
DMD-2 unit of butane treatment for 165 000 t/yr (5 500 bbl/day)
DMD-3 unit of naphtha treatment for 140 000 t/yr (4 000 bbl/day)
Serox-W unit of sulfur-alkaline waste water treatment for 2 000 t/yr
In operation since 2009
Treatment of gases of motor fuel hydrotreating for hydrogen sulfide
- Oil refinery in Syria, design of CAC (Germany) 2006
Treatment of butane-butylene fraction for hydrogen sulfide :
- J.S.”Taif-NK”, Nizhnekamsk, 2006
Plant for associated oil gas treating for hydrogen sulfide on Minnibaev USO of “TNGP” of J.S.”Tatneft”
Russia, TR, Almetyevsk, J.S.”Tatneft”.
In operation since 2004.
Capacity – 100 MM nm3/yr.
Hydrogen sulfide content:
- before treatment – 6% mole
- after treatment - <20 ppm
The design was developed by J.S.”Neftehimproekt”, Kazan.
Treatment of flare and associated oil gases and refluxes for hydrogen sulfide
Russia,
- J.S.”Salavatnefteorgsintez”,
- J.S.”Tatneft”,
- Novopolotskii refinery. In operation since 2002-2005.
Plant for reflux treating for hydrogen sulfide
Belarus, J.S.”NAFTAN”.
In operation since 2006.
Plant for butane-butylene fraction treating for hydrogen sulfide
Russia, Nizhnekamsk, J.S.”TAIF-NK”.
In operation since 2006.
Desulfurization plant of a compex for operation of gas field of South Middle area (SMAGP), Syria
Sirya, South Middle Area.
In operation since 2009.
Capacity – 500 MM m3/yr of natural gas.
Hydrogen sulfide content:
- before treatment – 0.25% mole
- after treatment - <0.0005% mole.
The design was developed by “Chemienlagenbau Chemnitz GmbH” (CAC), Germany.
Plant for refinery gases and refluxes treatment for hydrogen sulfide
Belarus, J.S.”NAFTAN”
In operation since 2010.
Capacity:
- for gases
of both units – 280 MM nm3/yr
- for refluxes
of straight-run and hydrocracking - 328 000 t/yr
of plant of delayed cocking - 62.8 000 t/yr
The design was developed by UNIS a.s. (AO) IOOO “UNIS nefteproekt”.
Dehydration, desalting and stabilization of oil:
- Oil preparation plant of Yaraktinsk oil field, Irkutsk oil company
- Oil preparation plant of Mordovoozersk oil field, Ulyanovsk
- Oil preparation plant of J.S.”Bogorodskneft”, Saratov, 1982-2005
AVT unit and automobile gasoline production
- Elkhov oil refinery of J.S.”Tatneft”, 1995-2005
Production of pentane-iso-pentane fraction
- J.S.”Salavatnefteorgsintez”, 1978-1981
Gas fractionation unit on catalytic cracking plants G-43-107, KT-1
- Moscow, Pavlodar, Ufa, Mazheikay, Mozyr refineries, 1984-1989
Production of propellent for aerosol packings
- «Tatneftegazpererabotka» of J.S.”Tatneft”, 2000-2005
Methods of measurement for analytic control of desulfurization and Claus processes on enterprises:
- J.S.”LUKOIL-PermNOS”, 2004
- J.S.”Yuzhno-Uralskaya promyshlennaya kompaniya”, 2004
- J.S.”Kuibyshev NPZ”, 2007
- ”Atyrau NPZ” Ltd., 2006-2007
- J.S.”Slavneft-YaNOS”, 2006
- J.S.”Salavatnefteorgsintez”, 2006
- J.S.”Otradnenskii GPZ”, 2007,2009
- ”Orenburg Gazprom Dobycha Ltd”, 2006,2007,2008,2010
- ”Naryanmarneftegaz Ltd.”,2009
- J.S.”TAIF-NK”. 2005, 2006, 2007, 2008, 2009
- J.S.”Ryazanskaya NPK”, 2009
- J.S.”SiburTyumenGaz”, 2010
- ”KINEF Ltd.”, 2010
- Research Institute of Petroleum Industry (Iran), 2005.
Proximate method of analysis of liquefied gas corrosivity in J.S.”Tatneft” in 2010.
Method of determination of argon, helium, hydrogen, methane, nitrogen, carbon oxide and carbon dioxide impurities in oxygen (”Tatneftegazpererabotka” of J.S.”Tatneft”, Almetyevsk, 2011).
Method of determination of a mass fraction of coke (carbon) on a coked and regenerated catalyst in thermocatalytic processes of petrochemistry and refinery for improvement of a target product quality (Gasoline plant of J.S.”TAIF-NK”, Nizhnekamsk, 2008).