IMPLEMENTATIONS

1. 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 MM t/yr (2 x 120 000 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.»

2. DMD-2 process (n-Pentane demercaptanization plant)
Russia, Novokuibyshevsk PCC
In operation since 1974
Capacity – 120 000 t/yr (3 800 bbl/day)

3. DMD-2 process (demercaptanization plant for fraction C2-C6)
Russia, J.S. «Salavatnefteorgsintez»
In operation since 1975
Capacity – 400 000 t/yr (12 700 bbl/day)

4. DMD-2 process (demercaptanization plant for fraction C2-C6)
Russia, J.S. «Salavatnefteorgsintez»
In operation since 1976
Capacity – 600 000 t/yr (19 000 bbl/day)

5. DMD-2 process (demercaptanization plant for butane-butylene fraction)
Russia, Samara Oil Refinery
In operation since 1977
Capacity – 130 000 t/yr (4 000 bbl/day)

6. 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

7. 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)

8. 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)

9. Serox-W process (plant for sulfur-alkaline waste water treatment)
Lithuania, Mazheikai Oil Refinery
In operation since 1990
Capacity – 25 m3/hr

10. Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Moscow Oil Refinery
In operation since 1990
Capacity – 30 m3/hr

11. 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)

12. Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Ryazan Oil Refinery
In operation since 1991
Capacity – 20 m3/hr

13. Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Pavlodar Oil Refinery
In operation since 1991
Capacity – 25 m3/hr

14. 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)

15. DMD-2 process (demercaptanization plant for LPG)
Russia, J.S. «Astrakhan Gasprom»
In operation since 1992
Capacity – 400 000 t/yr (13 000 bbl/day)

16. Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Omsk Oil Refinery
In operation since 1992
Capacity – 20 m3/hr

17. Serox-W process (plant for sulfur -alkaline waste water treatment)
Bulgaria, Burgas Oil Refinery
In operation since 1994
Capacity – 5 m3/hr

18. 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

19. 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)

20. Serox-W process (plant for sulfur-alkaline waste water treatment)
Russia, Yaroslavl Oil Refinery
In operation since 1999
Capacity – 20 m3/hr

21. DMC-3 process (plant for gas condensate demercaptanization)
Russia, Orenburg, J.S. «YUPK»
In operation since 2000
Capacity – 2 MM t/yr (40 000 bbl/day)

22. DMD-1 process (plant for kerosene demercaptanization)
Russia, Samara Oil Refinery
In operation since 2000
Capacity – 310 000 t/yr (6 500 bbl/day)

23. DMD-2 process (plant for fraction C2-C6 demercaptanization)
Russia, Perm Oil Refinery
In operation since 2000
Capacity – 300 000 t/yr (9 500 bbl/day)

24. 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)

25. DMC-1M process (plant for crude oil demercaptanization)
Kazakhstan, «CNPC-Aktobemunaigaz»
In operation since 2001
Capacity – 2.5 MM t/yr (50 000 bbl/day)

26. DMD-2 process (plant for fraction C2-C6 demercaptanization)
Russia, J.S. «Novokuibyshevsk Petrochemical Company»
In operation since 2002
Capacity – 150 000 t/yr (4 700 bbl/day)

27. DMC-3 process (plant for gas condensate demercaptanization)
Lithuania, J.S. «Mazheiku Nafta»
In operation since 2002
Capacity – 700 000 t/yr (14 000 bbl/day)

28. DMD-1 process (plant for kerosene demercaptanization)
Russia, Ukhta Oil Refinery
In operation since 2002
Capacity – 50 000 t/yr (1 000 bbl/day)

29. DMC-1M process (plant for crude oil demercaptanization)
Kazakhstan, J.S. «Kazakhoil Aktobe»
In operation since 2002
Capacity – 2.5 MM t/yr (50 000 bbl/day)

30. DMC-2 process (plant for condensate demercaptanization)
Latvia, J.S. «Stena» (crude oil tank farm)
In operation since 2003
Capacity – 150 m3/hr (22 500 bbl/day)

31. 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)

32. 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)

33. DMC-2 process (plant for gas condensate demercaptanization)
Russia, Taganrog, J.S. «Neklinovsknefteproduct» (crude oil tank farm)
In operation since 2004
Capacity – 150 m3/hr (22 500 bbl/day)

34. DMC-3 process (plant for crude oil demercaptanization)
Kazakhstan, J.S. «Kazakhoil Aktobe»
In operation since 2004
Capacity – 3 300 t/day (24 000 bbl/day)

35. DMD-3 + DMD-2 processes
(pilot plant for gasoline and LPG demercaptanization)
Iran, Tehran, Iranian Research Institute of Petroleum Industry «RIPI»
In operation since 2002
Capacity – 100 liters/hr (15 bbl/day)

36. DMC-1MA process (plant for heavy oil treatment for H2S + RSH)
Tatarstan, J.S. «Tatneft», NGDU «Nurlatneft»
In operation since 2005
Capacity – 4 900 t/day (34 000 bbl/day)

37. Serox-W process (plant for sulfur-alkaline waste water treatment)
Belorussia, Novopolotsk, J.S. «NAFTAN»
In operation since 2005
Capacity – 0.25 m3/hr

38. DMC-1 process (oil demercaptanization plant)
Kazakhstan, J.S. «KDO»
In operation since 2006
Capacity – 60 m3/hr (9 000 bbl/day)

39. DMD-2 process (demercaptanization plant for IBP-70°C fraction)
Russia, Nizhnekamsk, Gasoline Plant of J.S. «TAIF-NK»
In operation since 2007
Capacity – 300 000 t/yr (9 000 bbl/day)

40. 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)

41. Demercaptanization complex for naphtha and LPG
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.

42. DMC-3 process (Oil demercaptanization plant)
Kazakhstan, Uralsk, Chinarev NGKM, TOO “Zhaikmunai”.
In operation since 2008.
Capacity – 400 000 t/yr (8 000 bbl/day).

43. DMC-1 (Oil demercaptanization plant)
Kazakhstan, Aktyubinsk region, “Kaspiy neft” company.
In operation since 2010.
Capacity – 1 500 t/day (11 000 bbl/day).

44. DMC-3 process (Gas condensate demercaptanization plant)
Iran, Assaluye, Pars Oil and Gas Company (POGC).
To be put into operation in 2016.
Capacity – 3 trains each of 4 MM t/yr (3×80 000 bb/day).
The design was developed by RIPI and PetroSina Aria” companies.

45. DMD-2 ODORANT process
Iran, Assaluye,National Iranian Gas Company (NIGC).
To be put into operation in 2015.
Capacity:

  • Gas condensate – 600 000 t/yr (15 000 bbl/day)
  • Odorant – 800 t/yr.

The design was developed by “Iranian Engineering & Development Group”, Teheran.

46. Plant for adsorptive treatment of propane-butane fraction for aerosol packings
Russia, TR, Almetyevsk,OJS.”Tatneft”.
In operation since 2000.
Capacity – 10 000 t/yr.
The design was developed by PKO of “TNGP”.

47. Plant for ethanol amine treatment of associated oil gas for hydrogen sulfide on Minnibaev USO
Russia, TR, Almetyevsk, OJS”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.

48. Plant for ethanol amine treatment of flare gas for hydrogen sulfide

Russia, J.S.”Salavatnefteorgsintez”
In operation since 2005.

49. Plant for ethanol amine treatment of reflux for hydrogen sulfide

Belarus, J.S.”NAFTAN”.
In operation since 2006.

50. Plant for ethanol amine treatment of butane-butylene fraction for hydrogen sulfide

Russia, Nizhnekamsk, J.S.”TAIF-NK”.
In operation since 2006.

51. Plant for ethanol amine treatment of gases for hydrogen sulfide SMAGP field, 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.

52. Plant for ethanol amine treatment of refinery gases and refluxes 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 delayed cocking plant — 62 800 t/yr
The design was developed by UNIS a.s. (AO) IOOO “UNIS nefteproekt”.

53. Plant for oil treatment for hydrogen sulfide by purging with hydrocarbon gas with a unit for ethanol amine treatment of the purging gas
Russia, Nurlatneft, Sheshma UKPN,
In operation since 2015
Capacity:

  • for sales gas 2.1 MM t/yr
  • for treated gas 10.6 MM nm3/yr.

The design was developed by “Standartnefteproekt”, Kazan.

54. Serox-W process (Plant for Sulfur-Alkaline Waste Water Treatment)
Russia, Ryazan oil refinery, Ryazan.
In operation since 2014
Capacity 90 m3/hr.

55. Desulfurization plant of liquefied hydrocarbon gases
Belarus, RUP PO “Belarusneft”, Belarus gas refinery.
In operation since 2014.
Unit for adsorptive propane treatment
Capacity – 346 000 t/yr.

Unit for adsorptive butane treatment
Capacity – 205 400 t/yr

Unit for adsorptive treatment of dry stripped gas
Capacity – 3 460 kg/hr

OIL PREPARATION, OIL PROCESSING, GAS RACTIONATION

1. Technology of compressionless extraction of light hydrocarbons from oil
High-capacity plants in Ufa, Moscow, Kirishi, Nizhnekamsk, Omsk, Kstovo, Achinsk, Novokuibyshevsk, Belarus, Ukrane, Kazakhstan, more than 20 plants in total.
In operation since 1971.

2. Modification of gas fractionation section of GO-4 plant
Russia, Salavat
In operation since 1980.

3. Plant for complex oil preparation of OJS “Tatneft”
Periof of modification 1982-2005
Capacity 1.8 – 3.3 MM t/yr.

4. Modification of gas fractionation sections of complexes
of Moscow, Pavlodar, Ufa, Mozheikai, Mozyr refineries.
In operation since 2000.

5. Modification of section S-100 of Elhov NPU of OJS”Tatneft”
Russia, Almetievsk,
In operation since 2001
Capacity 500 000 t/yr
The design was developed by OJS “Neftekhimproekt”, Kazan.

6. Plant for oil preparation of OOO”Irkutsk oil company”
Russia, Irkutsk, Yaraktinsk oil field
In operation since 2004
Capacity800 000 t/yr
The design was developed by OJS “Neftekhimproekt”, Kazan.

7. Plant for oil preparation of ZAO “Bogorodskneft”
Russia, Saratov,
In operation since 2006
Capacity400 000 t/yr
The design was developed by OJS “Neftekhimproekt”, Kazan.

8. Plant for oil preparation of OJS “Udmurtneft”
Russia, Udmurtiya, Votkinsk
In operation since 2008
Capacity 1 400 000 t/yr
The design was developed by OJS “Neftekhimproekt”, Kazan.

9. Plant for oil preparation of “Suleevneft NGDU”
Russia, Almetyevsk, OJS “Tatneft”
In operation since 2009
Capacity 1 000 000 t/yr
The design was developed by OJS “Neftekhimproekt”, Kazan.

10 Section for benzene separation from reforming catalyzate for production of sales gasoline with benzene content no more than 1% on Elkhov NPU

Russia, Almetievsk, OJS “Tatneft”
In operation since 2012
Capacity 47 700 t/yr
The design was developed by OJS “Tekhnoproekt”, Novokuibyshevsk.

OIL PREPARATION, OIL PROCESSING, GAS RACTIONATION

1. Technology of compressionless extraction of light hydrocarbons from oil
High-capacity plants in Ufa, Moscow, Kirishi, Nizhnekamsk, Omsk, Kstovo, Achinsk, Novokuibyshevsk, Belarus, Ukrane, Kazakhstan, more than 20 plants in total.
In operation since 1971.

2. Modification of gas fractionation section of GO-4 plant
Russia, Salavat
In operation since 1980.

3. Plant for complex oil preparation of OJS “Tatneft”
Periof of modification 1982-2005
Capacity 1.8 – 3.3 MM t/yr.

4. Modification of gas fractionation sections of complexes
of Moscow, Pavlodar, Ufa, Mozheikai, Mozyr refineries.
In operation since 2000.

5. Modification of section S-100 of Elhov NPU of OJS”Tatneft”
Russia, Almetievsk,
In operation since 2001
Capacity 500 000 t/yr
The design was developed by OJS “Neftekhimproekt”, Kazan.

6. Plant for oil preparation of OOO”Irkutsk oil company”
Russia, Irkutsk, Yaraktinsk oil field
In operation since 2004
Capacity800 000 t/yr
The design was developed by OJS “Neftekhimproekt”, Kazan.

7. Plant for oil preparation of ZAO “Bogorodskneft”
Russia, Saratov,
In operation since 2006
9. Capacity400 000 t/yr
10. The design was developed by OJS “Neftekhimproekt”, Kazan.

8. Plant for oil preparation of OJS “Udmurtneft”
Russia, Udmurtiya, Votkinsk
In operation since 2008
Capacity 1 400 000 t/yr
The design was developed by OJS “Neftekhimproekt”, Kazan.

9. Plant for oil preparation of “Suleevneft NGDU”
Russia, Almetyevsk, OJS “Tatneft”
In operation since 2009
Capacity 1 000 000 t/yr
The design was developed by OJS “Neftekhimproekt”, Kazan.

10. Section for benzene separation from reforming catalyzate for production of sales gasoline with benzene content no more than 1% on Elkhov NPU

Russia, Almetievsk, OJS “Tatneft”
In operation since 2012
Capacity 47 700 t/yr
The design was developed by OJS “Tekhnoproekt”, Novokuibyshevsk.

11. ELOU-AVT-2 plant (Technical re-equipment for oil capacity increase)
Russia, Tyumen, OJS “Antipinskiy NPZ”
In operation since 2013.
Capacity — 3.3 MM t/yr.
The design was developed by OJS “Neftekhimproekt”, Kazan.

12. Modification of plant for oil preparation of OJS “Udmurtneft”
Russia, Udmurtiya, OJS “Udmurtneft”, Kiengop field.
In operation since 2013.
Capacity:

  • Emulsion CDNG-1 – 6 787 000 m3/yr.
  • Emulsion CDNG-2 – 1 737 000 m3/yr.

The design was developed by OJS “Neftekhimproekt”, Kazan.

13. Complex plant for primary oil processing, bitumen production and a unit of afterburning furnaces for oxidation gases (scientific and technical re-equipment)
Russia, Surgut, OJS “Surgutneftegaz”.
In operation since 2013.

Экспресс-метод анализа коррозионной активности сжиженных газов в ОАО «Татнефть» в 2010 г.

Метод определения примеси аргона, гелия, водорода, метана, азота, оксида и диоксида углерода в кислороде (Управление «Татнефтегазпереработка» ОАО «Татнефть» им. В.Д. Шашина, г. Альметьевск, 2011 г.)

Метод определения массовой доли кокса (углерода) на закоксованном и регенерированном катализаторе в термокаталитических процессах нефтехимии и нефтепереработки для улучшения качества целевого продукта (Завод бензинов ОАО»ТАИФ-НК», г.Нижнекамск, 2008 г.)

Нормативы технологических потерь нефти и нефтепродуктов и расхода топлива на 36 нефтеперерабатывающих предприятиях.

Методика определения компонентного состава попутного нефтяного газа (Управление «Татнефтегазпереработка» ОАО «Татнефть», 2013 г.)

Методика определения компонентного состава отопительного газа (ОАО «Ангарская нефтехимическая компания», 2012 г.)