ÀÇÑíåôòåáàçñòðîé

Phone:
+79257729344

E-mail: azsstroy@mail.ru
Home     About company     Contact Details     Our Clients

Mini Oil Reprocessing Plant

Installing UPN (refining upgraded whirlpool)

The firm "AZSNEFTEBAZSTROY" can offer installations of AT series "NP-MV" - upgraded oil, swirl, designed for processing of hydrocarbons, as well as the installation type AT + PPG-technology series "NP-LOF" upgraded oil, swirl, deep processing, allowing increase the yield of light hydrocarbons (gasoline, kerosene, diesel fuel, etc.) to 70-80%.

At the request of customers install NP-IDP can be adjusted to produce different bitumen.

Product Overview and Technical Data series units "NP-MB."

Compact modular plant distillation of hydrocarbons - "NP-MV" (hereinafter - unit) - a set of sporadically produced technologically and structurally related block equipment for the processing of hydrocarbon raw materials for light distillate fractions by distillation and subsequent condensation of vapor light fractions and their cooling following close-up of:

  1. block heating raw materials *
  2. tubular heater *
  3. gasoline unit *
  4. diesel unit *

Material and equipment installation are defined statement of work. The unit is designed and includes as standard equipment in the production of the primary processing of hydrocarbons, according to the working draft.

Additionally, the composition of production for the primary processing of raw materials, as a rule, are:

  1. unit process pumps;
  2. tank farm with process piping system;
  3. Risers liquid;
  4. block the introduction of anti-knock additives and compounding;
  5. technological capacity;
  6. water recycling system;
  7. steam is the system;
  8. Candle dispersion;
  9. fire extinguishing system;
  10. system of main and emergency power;
  11. industrial system of sanitation;
  12. laboratory;
  13. industrial and domestic premises, etc.

The specific composition and production equipment for the primary processing of hydrocarbons determined project, developed in accordance with the applicable rules and regulations, the parameters of the feedstock, the binding conditions at the location, requirements to get the product and other necessary parameters.

Parameter name

Value

The initial product

different types of oil and gas condensate

The resulting products

Fractions: gasoline, kerosene, diesel or heating oil, fuel oil and bitumen to install NP-IDP

Annual capacity on conditional raw, roughly, tons / year

25-30, 50-70, 100-150, 200-250

Operating pressure, MPa (kgf/cm2), not more

0,07 (0,7)

Temperature, °C, not more

300-3500°C

The temperature of the finished product at the outlet in the tank °C, not more than:
faction
evaporated waste

40-60*

75*

Main voltage protection, in

380

The installed electric power in kW

40 -200* kW

Environment

Nonaggressive flammable, explosive, low risk (Hazard Class 4 according to GOST 12.007)

Installation class

V1G

Area for loading, m

Determined by the project

Installation Size, mm

Determined by the project

Weight, t

  25 – 70*

*The value is determined by the parameters of raw and refined detail design installation.

General information on the "PPG-technology" used in installations series "NP-IDP"

The unit is designed for processing the distillation residue (oil) produced by devices such as the AT series "NP-MV", based on "PPG - technology," which allows you to bring the depth of processing of HC to 70-80%.

 The essence of "PPG - Technology" is to conduct thermolysis raw materials using a special activating effects as technological methods, enabling a selective effect on the individual groups of hydrocarbons under thermolysis. Impacts are based on the submission to the pre-reaction zone of the activating gas recycle stream certain fractions of hydrocarbons and recycle water-soluble metal salts, which makes changes to the dispersion stability of liquid hydrocarbons, and greatly intensifies the process of destruction of the heavy fractions at temperatures too low to intensive processes of polycondensation ( coking).

These reactions occur at relatively low temperatures - 370-450 ° C. Are most easily cracked paraffinic hydrocarbons, and the most difficult - aromatic hydrocarbons. Naphthenic hydrocarbons are intermediate.

In addition to reducing the temperature degradation processes of heavy hydrocarbons, gas bubbles intensify the evaporation of light fractions, effectively taking them out of the reaction zone, and the recycle of heavy metal salts factions, working as catalysts give a general elevation of products allow them to get much closer in quality to the modern requirements of a motor fuel. Also, there is a reduction of viscosity, sulfur and nitrogen compounds, removal of heavy metals.

      Thus, the use of the described process can significantly reduce the cracking temperature - up to 450 ° C and below, to avoid unwanted coking equipment, and the process be carried out at low pressure.

Thermomechanical effects on raw material applied in the new technology, keeps aggregate stability of the reaction mixture, even at high concentrations of asphaltenes. This allows, on the one hand, a large degree of conversion of heavy hydrocarbons into light oil, on the other hand, get a residual product concentrated colloidal solution of resins and asphaltenes - the ideal basis for the production of non-oxidized bitumen of different brands.

 

Material balance "PPG - Technology" *

Table 2

Raw materials processed

Processed products, wt%.

The temperature in the reactor,
°С.

gas

gasoline

diesel

gasoil

balance

Atmospheric residue
(Fuel oil)

1/5

8/15

45/55

15/20

15/30

370/400

Vacuum residue
(tar)

2/5

5/8

40/45

10/18

30/45

400/420

Heavy crude

2/4

8/18

40/50

³10

25/40

370/400

 

* Experts' AZSNEFTEBAZSTROY "This process is constantly reviewed and improved, which allows to obtain guaranteed results to the output of light hydrocarbons.

Table 3 shows the results of the processing of straight oil with Urengoy field. It is shown that by varying the parameters of activation, you can significantly change the output of refined products, which are light and gas oil fractions, with the balance of fuel oil is obtained. These data are the results of working out a pilot plant with a capacity of 2 tons per hour of raw material at the operating temperature of 390 °C

Table 3

Mode

Activation

Conclusions fractions,% weight / kg / h

+ Gas conversion loss

BKF

Diesel

Gasoil

Balance

soft

2,6

55,5

4,6

100

25

536

44,8

960

23

490

average

4

86

6

129

31,5

676

36,5

783

22

472

hard

5

107

15

322

52

1115

8

172

20

429

For an example, the calculation made for one of the customers, increase the yield of light oil in the application of PPG technology in conjunction with the installation of the AT. Depth of processing is taken at the level of 70-80%

Trade balance of the plant capacity of 100 thousand tons per year (ThTpY).

Name

Product yield after NP-MB-100

Product yield after "PPG-technology" (NP-MVU-100)

All with the unit

ton

%

ton

%

ton

%

Arrives, t

Crude

100 000

100

100 000

100

Masut

47 000

100

Produced, t

Gasoline A-76

18 000

18,0

13 000

27,7

31 000

31

Kerosene

5 000

5,0

5 000

5

Diesel fuel

28 000

28,0

18 000

38,3

46 000

46

Only light

51 000

51

82 000

82

Masut

47 000

47,0

Bitumen

15 000

31,9

15 000

15

Losses

2 000

 2,0

1 000

2,1

3 000

3

Total:

100 000

100

47 000

100

100 000

100

At the rate it is clear that the yield of light hydrocarbons, in the application, "PPG-technology" increases by 1.6 times, with an increase in the cost of installation of 1.46 times.

- Depending on the feedstock column equipment manufactured by one or two-column scheme, also used plates of original design, to maximize the efficiency of the column, to the built-in or separate stripping;

- Tube furnace is made to reflect the latest developments in the field of heat transfer, which allows the best use of the furnace coil;

- Used to install pumps with variable speed;

- Control and measuring devices equipment and apparatus manufactured on modern components and allows you to control the manufacturing process of any settlement;

- Term of production equipment for 3-5 months (for installations NP-MV and NP-MVU).

The cost of installations of AT Series NP-MB (RR)

 

Name

NP-MB-10

(10-15 ThTpY)

NP-MB-20

(18-22 ThTpY)

NP-MB-25

(25-30 ThTpY)

NP-MB-50

(50-70 ThTpY)

NP-MB-100

(100-150 ThTpY)

NP-MB-200

(200-250 ThTpY)

1

Column equipment

1.8

4.6

4.6

5.4

9.1

18.2

2

Tube furnace

2.2

6.2

6.4

8.7

10.4

21.7

3

Heat Transfer Equipment

1.8

6.5

7.6

9.5

11.2

29.9

4

Technological capacity

1.5

1.5

1.5

2.1

2.2

4.1

5

Steam generator with water treatment system

0.9

1.3

1.6

2.2

2.1

2.4

6

Process Pumps

1.5

1.7

1.7

2.8

6.8

12.9

7

Control and measuring devices equipment and apparatus

2.9

5.2

5.6

6.4

6.0

9.7

8

Other equipment (candle dispersion process piping, etc.)

1.1

1.3

1.7

2.2

2.5

5.7

9

Installation and commissioning

1.8

2.6

3.6

4.3

6.3

10.8

10

Design work, built documentation

3.6

3.9

5.2

6.1

8.3

11.7

11

Total *:

19.1

34.8

39.5

49.7

64.9

127.1

* Approximate cost units, the real value of blocks is determined by the stage of pre-investment period.

The cost of the AT + "PPG-technology" Series NP-MVU (RR)

Name

NS-IDP-25

(25-30 ThTpY)

NS-IDP-50

(50-70 ThTpY)

NS-IDP-100

(100-150 ThTpY)

NS-IDP-200

(200-250 ThTpY)

1

Column equipment

5.1

6.2

10.9

19.5

2

Tube furnace

6.5

9.9

12.7

23.3

3

3K-block installation process (NP-IDP) *

16.6

28.6

37.1

63.9

4

Heat Transfer Equipment

8.6

11.8

14.9

32.1

5

Technological capacity

1.7

2.3

2.6

4.4

6

Steam generator with water treatment system

2.1

2.5

2.4

2.6

7

Process Pumps

2.3

3.2

8.3

13.8

8

Control and measuring devices equipment and apparatus

6.3

6.6

7.6

10.4

9

Other equipment (candle dispersion process piping, etc.)

1.8

2.5

3.1

6.2

10

Installation and commissioning

4.1

4.9

7.6

10.0

11

Design work, built documentation

5.8

6.8

10.1

12.5

12

Total *:

60.9

85.3

117.3

198,7

 

MINI GAS PROCESSING PLANTS

Research and Development Centre named after Nikola Tesla, Ioshkar Ola; AZSNEFTEBASTROI, Moscow; and New Petroleum Technologies LLC, Stavropol offer mini Gas Processing Plants (MGPPs).

In this presentation, we provide a complex with improved technologies that fundamentally differ from the existing ones. This enables to tackle different tasks relating to the processing of hydrocarbons. The unit can have different throughput capacity based on customer’s wish.

A MGPP is intended for the processing of associated petroleum gases (APG) to liquid hydrocarbons. The process is based on the Lebedev’s synthesis conversion that takes place in the SHF fields. The feedstock is water + associated petroleum gas (APG); intermediate products are water + acetylene, the output product is a mixture of C1-C5 alcohols and C5-C12 hydrocarbons.

The alkylation reaction that has been used in the chemical and hydrocarbon process industries is the essence of the process. The reaction proceeds using catalysts at temperatures of 530-560оC and at the pressure of 10 atm. The main device is a tube reactor (with a diameter of 200-250 mm and a length of 1.5-2.5 m). At least two of these reactors will be installed to provide regeneration of the catalyst. A bigger output of heavy hydrocarbons can be achieved if the number of the reactors is increased to 4 or 6.

The received mixture of hydrocarbons and alcohols is fed to the oil treatment unit while a part of the alcohols (methanol-butanol) is dissolved in the stratum water and together with the latter it is pumped into the productive strata. The presence of the alcohols in the water must improve the wash-off properties and increase the oil displacement efficiency; however, this aspect has not been considered yet. The residual alcohols and liquid hydrocarbons will be dissolved in the oil and realized together with the latter.

Advantages of the offered MGPPs are as follows:

  1. Reliability of operation, 10-year resource.
  2. Reliability of operation, 10-year resource.
  3. Safety. Reliable automatic system based on the components manufactured both at home and abroad will exclude emergency situations when operating the unit, enable to manage and control the operation of the unit, as well as receive current technological process data from any populated locality.
  4. Modules of the modular unit can be transported by any types of transport.
  5. The project provides maximum possible use of customer’s existing infrastructure.

When the microwave processing rate of a chemical reaction increases a hundred times or more, the reaction time is reduced by the same amount. Plants are compact, less metal content of equipment, respectively, significantly reduced cost.

These technologies provide products complying with Euro-3, 4.

 

Three column of the 25 tons tons per year

Five column of the 25 Comrades per year

Pump unit

Block refrigerators

Our developments are based both on the traditional oil refinery practices and the experience gained in other fields.

The design based on all the foregoing enables to more accurately understand, model and  perform technological processes. These solutions are protected by the patents of the Russian Federation; and the process of obtaining foreign patents is in progress.

Thus, AZSNEFTEBAZSTROY is ready to act as an engineering,

company for the construction of oil refineries, consolidate and successfully implement the potential of domestic and foreign developments in the field of oil refinery

 


    Our address: 57(B) Baryshikha street, Moscow, Russia
   Open Map

    Phone:  +79257729344