Rudin M.G., Smirnov G.F. Design of oil refineries and petrochemical plants
8. FIRE COMMUNICATIONS AND ALARMS. METHODS AND MEANS OF FIRE PROTECTION AND FIRE FIGHTING
8.1. The buildings of fire stations and fire posts are built according to existing standard designs approved in the prescribed manner, as well as according to individual projects with the appropriate permission.
8.2. The number and location of fire station buildings and fire posts and the territory for them are determined in accordance with the chapter of SNiP "General plans of industrial enterprises. Design standards" taking into account the service radius.
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Note. The number and type of fire trucks are determined by local fire departments and departments.
8.3. The buildings of fire stations and fire posts of enterprises must be connected by direct telephone communication with the city fire department, the switchboard of the enterprise telephone exchange and the booster pumping station of the fire water supply system. If enterprises have two or more fire station buildings and fire posts, they must be connected to each other by two-way direct telephone communication.
8.4. Industrial, administrative, warehouse and auxiliary buildings, outdoor installations, warehouses (parks) and unloading racks must be equipped with electric fire alarm detectors to call the fire department.
8.5. General purpose electrical fire alarm detectors must be installed:
in outdoor installations and open warehouses of categories A, B and C - along the perimeter of the installation, warehouse no more than 100 m apart;
in warehouses (parks) - flammable gases, flammable and combustible liquids - along the perimeter of the embankment no more than 100 m apart;
on unloading racks for liquefied hydrocarbon gases, flammable and combustible liquids - every 100 m, but not less than two (at the stairs for servicing the racks).
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Note. Manual fire call points are installed regardless of the presence of automatic fire alarm call points.
8.6. General purpose electric fire alarm detectors must be located at a distance of at least 5 m from the boundary of the installation or warehouse embankment.
8.7. Fire alarm receiving stations must be installed in fire station buildings.
8.8. Industrial and warehouse buildings must be equipped with automatic fire extinguishing and fire alarm systems in accordance with the lists approved by the Ministry of Petroleum and Chemical Industry of the USSR and agreed upon with the Main Directorate for Promotion of the Ministry of Internal Affairs of the USSR and the State Construction Committee of the USSR (Appendix 1), chapters of SNiP and other regulatory documents.
8.9. Fire monitors are installed:
a) in external explosion- and fire-hazardous installations for the protection of apparatus and equipment containing flammable gases, flammable and combustible liquids;
b) in raw materials, commodity and intermediate warehouses (parks) to protect spherical and horizontal (cylindrical) tanks with liquefied flammable gases, flammable and combustible liquids;
c) on railway unloading racks and river berths of LPG, LVZh and GZh.
Furnaces and devices operating at temperatures above 450 o C (recovery boilers, furnaces, pressure furnaces, reactors, etc.) are not subject to protection by fire monitors. When installing fire monitors near this equipment, limiters must be provided for the rotation of these monitors towards devices heated to a temperature of more than 450 o C.
8.10. Monitors are usually installed with a permanent connection to the high-pressure water supply network. In cases where the water supply at an existing enterprise does not provide the pressure and water flow necessary for the simultaneous operation of two fire monitors, the latter must be equipped with devices for connecting mobile fire pumps.
8.11. Monitors should be installed with a nozzle diameter of at least 28 mm. The pressure at the nozzle must be at least 0.4 MPa (40 m of water column).
8.12. The number and location of monitors to protect equipment located in an outdoor installation is determined graphically, based on the conditions of irrigation of the protected equipment with one compact jet.
8.13. The number and location of monitors to protect tanks in a warehouse (park) is determined from the condition of irrigation of each tank with two jets, and in the presence of a stationary irrigation system - with one jet.
8.14. Tanks with flammable liquids and gas liquids with a volume of 5000 m 3 or more, regardless of the height of the tank walls, must have stationary water irrigation installations.
Tanks with liquefied hydrocarbon gases and flammable liquids stored under pressure must have automatic stationary water irrigation systems.
8.15. Outdoor installations with a height of 10 m or more must be equipped with dry pipe risers with a diameter of at least 80 mm to reduce the time for supplying water, foam and other fire extinguishing agents.
Each outdoor shelf with a length of more than 80 m must have at least two risers located near the flight of stairs. On the dry pipe riser on each floor there must be shut-off and connecting valves designed for the operation of hoses DN 80. On the dry pipe risers, drain valves should be provided to empty them of water.
8.16. For buildings with a height of more than 15 m, dry pipes with connecting heads at both ends with a diameter of at least 80 mm should be provided along the fire escapes to the roof. On vertical fire escapes, one of the strings can be made in the form of a dry pipe.
8.17. Buildings and structures of enterprises must be provided with primary fire extinguishing means in accordance with the “Standard Fire Safety Rules for Industrial Enterprises” and the requirements of industry standards.
8.18. Fire-fighting water supply to enterprises must be provided taking into account the requirements of the SNiP chapters "Water supply. External networks and structures" and "Internal water supply and sewerage of buildings. Design standards", as well as the requirements of this section.
8.19. As a rule, enterprises should design an independent fire-prevention water supply system. The pressure in the network must ensure the ability to operate fire-fighting devices (monitors, sprinklers, etc.), but be at least 0.6 MPa (6 kgf/cm2).
8.20. The water consumption for fire extinguishing from the fire-fighting water supply network should be taken based on two simultaneous fires at the enterprise:
one fire in the production area;
the second fire - in the area of raw materials or commodity warehouses (parks) of flammable gases, flammable and combustible liquids.
8.21. Water consumption for fire protection and fire extinguishing from the fire-fighting water supply network is determined by calculation, but must be taken at least:
for the production area - 170 l/s;
for commodity warehouses (parks) - 200 l/s.
8.22. The water flow from the fire-fighting water supply must ensure extinguishing and protection of equipment by both stationary installations and mobile fire equipment.
8.23. When calculating the performance of a fire-fighting water supply system, it should be taken into account that in addition to water consumption for stationary installations, it must provide a water supply of at least 50 l/s. for mobile fire fighting equipment or simultaneous operation of two fire monitors.
In cases where the water consumption for the simultaneous operation of two monitors exceeds 50 l/s, it is necessary to take into account the water consumption only for the operation of the monitors.
8.24. Water consumption for stationary irrigation installations should be taken as follows:
a) for open technological installations - for column-type devices, based on the sum of water consumption for cooling a conditionally burning column and adjacent columns located at a distance of less than two diameters of the largest burning one or adjacent to it;
b) for commodity and raw materials and intermediate warehouses (parks) with spherical tanks of LPG and flammable liquids stored under pressure, for simultaneous irrigation of a conditionally burning tank and adjacent tanks located at a distance of the diameter of the largest burning or adjacent tank or less, and for horizontal - according to table. 6.
Table 6
Number of simultaneously irrigated horizontal tanks
| Tank locations | Volume of a single tank, m 3 | |||||
| 25 | 50 | 110 | 160 | 175 | 200 | |
| In one row | 5 | 5 | 5 | 5 | 3 | 3 |
| In two rows | 6 | 6 | 6 | 6 | 6 | 6 |
8.25. The intensity of water supply for cooling the surface of equipment for stationary irrigation installations should be taken in accordance with Table. 7.
Table 7
| Name of devices | Water supply intensity, l/(m 2 *s) | |
| 1 | Spherical and cylindrical tanks with liquefied flammable gases and flammable liquids stored under pressure: | |
| a) surfaces of tanks without fittings | 0,1 | |
| b) surfaces of tanks at the locations of fittings | 0,5 | |
| 2 | Column-type devices with LPG and flammable liquids | 0,1 |
8.26. Protection of column apparatus at a height of up to 30 m should be carried out by fire monitors and mobile fire fighting equipment. When the height of column apparatus is more than 30 m, their protection should be carried out in combination, namely: up to a height of 30 m - with fire monitors and mobile fire equipment, and above 30 m - with stationary irrigation installations.
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Note. In cases where the protection of column devices with monitors is impossible (other devices interfere), they should be protected with stationary irrigation installations for the entire height.
8.27. A water supply pumping station with fire pumps serving tank farms with LPG, flammable liquids and flammable liquids must be located at a distance of at least 50 m from the pumping stations for pumping LPG, flammable liquids and flammable liquids and at least 100 m from the tanks.
8.28. The supply of water for fire protection of technological installations, commodity and raw materials and intermediate warehouses, unloading racks must be stored in at least two reservoirs located at the fire-fighting water supply pumping station.
8.29. In addition to the fire-fighting water supply system at oil refineries, it is necessary to provide for the construction of the following located one from the other at a distance of no more than 500 m:
In the area of tank farms - fire reservoirs with a capacity of at least 250 m 3.
In the area of production installations - wells with a capacity of 3 - 5 m 3 with water supplied to them from the industrial water supply network through a pipeline with a diameter of at least 200 mm with the possibility of drawing water from them by two fire engines or hydrants installed on the industrial (recycling) water supply network.
8.30. The distance from places where water is taken from fire reservoirs must be at least:
To buildings and structures of categories A, B and C for fire danger - 20 m;
To tanks with liquefied hydrocarbon gases and flammable liquids - 60 m;
To tanks with flammable liquids - 40 m.
8.31. Reception wells of reservoirs and reservoirs-wells should be located at a distance of no more than 2 m from the side of highways or have entrances from them with a platform of 12-12 m.
8.32. The top of hydrant wells must be higher than the grading level of the area adjacent to the road. Roadsides near hydrants must have a hard surface (compacted with crushed stone, impregnated with bitumen) for a length of at least 20 m (10 m on both sides of the hydrant). The distance between hydrants should be no more than 100 m.
For individual structures of categories D and D (flare installation, open storage of non-combustible materials, etc.), it is allowed to provide fire hydrants on dead-end fire water supply lines with a length of no more than 200 m.
8.33. If the enterprise has a cooling tower, it must be accessible from the highway with an area of at least 12-12 m in size to be able to use the cooling tower basin as a reserve reservoir for supplying water for fire extinguishing.
8.34. Extinguishing of organoelement compounds must be carried out in accordance with the “Safety Rules for the production of organoelement compounds”.
8.35. In pumping rooms of categories A, B and C, equipped with a stationary automatic fire extinguishing system with a six-fold supply of foam concentrate, the installation of an internal fire-fighting water supply system may not be provided. In this case, it is necessary to install internal fire hydrants and manual foam nozzles on the supply pipelines of the fire extinguishing system.
8.36. Pumping rooms pumping flammable liquids and gases with a volume of up to 500 m 3 must be equipped with stationary steam extinguishing systems, if a stationary foam extinguishing system is not provided.
8.37. The stock of foaming agents at the enterprise is calculated based on the required intensity of supply of the foaming agent solution to extinguish two design fires. In addition, the enterprise must have a 100% reserve that can be used for mobile equipment.
8.38. The stock of foaming substances at the enterprise must be stored in special premises - warehouses for storing fire extinguishing agents, located in the area of tank farms for flammable and combustible liquids and production plants with access to the warehouses from roads. Premises for storing fire extinguishing agents must be dry, heated, with an indoor air temperature in winter not lower than +5 o C, have ventilation with deflectors and connection to a sewerage system and electric lighting. It is allowed to store the foam concentrate in heated containers located outside buildings.
8.39. Protection of technological furnaces in case of accidents and fires, as well as extinguishing fires inside furnaces when pipes burn out, is carried out in accordance with the “Instructions for the design of steam protection of technological furnaces at oil refining and petrochemical industry enterprises”.
8.40. Steam extinguishing systems must be connected to permanently operating industrial steam pipelines of the enterprise.
The location for connecting the steam extinguishing system to permanently operating production steam pipelines at technological installations is selected within the given installation, and to the steam pipeline network of the enterprise - within no more than 50 m from the boundary of the installation or facility.
The steam extinguishing system must be connected through two valves installed in series (or two valves) with a control tube with a valve installed between them.
8.41. To extinguish a fire in steam extinguishing systems, saturated, spent (crumpled) water steam or superheated steam for technological purposes can be used. At the same time, saturated water vapor is more effective for fire extinguishing compared to superheated steam.
8.42. Steam extinguishing can be carried out using stationary and semi-stationary steam pipeline systems (installations).
Stationary steam extinguishing systems include steam pipeline systems that supply steam directly to the protected object.
Semi-permanent steam extinguishing systems include steam pipeline systems that supply steam to the territory of the production plant and end with external steam extinguishing risers with outlets for connecting hoses for supplying steam to places of possible fires.
8.43. Stationary steam extinguishing systems should be used in industrial premises with a volume of no more than 500 m 3, which contain apparatus and equipment with flammable and combustible liquids, for example, in process pumping rooms, in pipe trays laid within industrial premises.
8.44. Semi-permanent steam extinguishing systems should be used on external process installations, for example, on columns and other apparatus.
To extract steam for fire extinguishing, risers with a nominal diameter of at least 40 mm must be provided at a distance of no more than 30 m from one another.
The steam pressure at the risers should be no more than 0.6 MPa (6 kgf/cm2). Portable hoses can be used with a diameter of 20 mm with watering trunks or other nozzles.
The hoses must be connected to the risers manually, without the use of tools, using a union nut with a handle or a “brush”.
8.45. Shut-off devices on steam extinguishing lines (valves, gate valves) must be located in easily accessible places, outdoors, at a height of 1.35 m from the site level.
8.46. Perforated pipes are used as internal steam distribution pipelines for stationary steam extinguishing systems in enclosed spaces. Holes in perforated pipes for steam release should be 4-5 mm in diameter. To drain condensate from steam supply lines and steam inlets, drains must be provided, located in the lowest places along the slope of the pipes in such a way that both condensate and steam jets do not interfere with the actions of operating personnel.
8.47. To supply steam to enclosed spaces, perforated pipes are laid along the entire internal perimeter of the room at a height of 0.2-0.3 m from the floor. In this case, the pipe openings are located so that the steam jets coming out of them are directed horizontally into the room.
8.48. When calculating steam extinguishing systems, the intensity of steam supply is taken as the main indicator. Estimated fire extinguishing time 3 minutes.
The intensity of steam supply is understood as the amount of steam supplied to enclosed spaces or tightly closed technological units per unit time per unit volume filled with steam (kg/s*m3).
The calculated intensity of steam supply (superheated and saturated) for volumetric steam extinguishing is given in table. 8.
Table 8
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Note. For closed objects, the calculated value is their total internal volume.
8.49. Inert gases (nitrogen, carbon dioxide, argon, etc.) can be used to extinguish fire both in enclosed spaces and in open installations.
8.50. Fire extinguishing (burning) with inert gas is based on:
a) to reduce the oxygen concentration in the air of industrial premises and around the combustion site (stationary fire extinguishing systems);
b) on knocking down the flames of ignited gases and vapors with a jet of inert gas) in case of leakage through formed leaks in apparatus and pipelines (semi-permanent fire extinguishing systems).
8.51. In open installations, extinguishing with inert gas is based on knocking down the flame of ignited gases and vapors with a jet of inert gas.
8.52. To knock down the flames of ignited gases and vapors with a jet of inert gas, both in buildings and in open installations, process inert gas must be used.
8.53. The inert gas pressure at the risers should be no more than 0.6 MPa (6 kgf/cm2).
8.54. To select inert gas for fire extinguishing in premises, on process pipelines with inert gas at a distance of no more than 30 m from one another, pipes with a nominal diameter of at least 20 mm with shut-off valves must be provided.
8.55. In open installations, risers with a nominal diameter of at least 40 mm must be installed at a distance of no more than 30 m from one another, which are connected to the inert gas technological networks.
8.56. At the 1.35 m mark of each site, the risers must be provided with pipes with a nominal diameter of at least 20 mm with shut-off valves.
50% of the total number of pipes must be provided with rubber-fabric hoses with an internal diameter of at least 25 mm, meeting the requirements of GOST "Steam hoses". The location of pipes and hoses must be indicated in the working drawings of the equipment location.
8.57. Stationary extinguishing devices with inert gas, based on the principle of reducing the oxygen concentration in the air, can be used for closed volumes such as chambers and compartments, where extinguishing with steam is not economically feasible, or steam, as a fire extinguishing agent, cannot provide the appropriate effect during extinguishing.
General information about the design of industrial enterprises.
The value of design estimates documentation.
Organization of design.
Basis for the development of design and estimate documentation1.
Types and nature of construction.
Selection of construction site.
Design assignment.
Basic initial data for design.
Development of design and estimate documentation.
Coordination, examination and approval of projects.
Cost and financing of design and survey work.
Regulatory. design duration.
Development of the technological part of the refinery and petrochemical plant project.
Modern schemes for oil refining and petrochemical production.
Main types of processed raw materials.
Initial data for developing the technological part of the project.
Drawing up material balances of production and material flow diagrams of the plant.
Use of computer technology to draw up diagrams and balances of plants.
Commodity balance of the plant.
Determining the need for reagents, catalysts, compressed air, nitrogen, hydrogen.
Occupational safety and health.
Design of the technological part of installations and workshops.
Technological installations included in the plant.
Initial materials for designing a process plant.
Development of a technological scheme for the installation.
Technological tasks for related specialists.
Design of equipment piping.
Equipment layout.
Drawing up custom specifications.
The procedure for drawing up and processing applications for the development of new types of equipment.
Procedure for using equipment containing scarce metals.
Fundamentals of technological calculation of apparatus and equipment.
Calculation of reactors.
Calculation of distillation columns.
Calculation of absorption columns.
Calculation of heat exchangers.
Calculation and selection of tube furnaces.
Calculation and selection of pumps.
Calculation and selection of compressors.
Design of general plant facilities.
Reception and storage of raw materials.
Preparation of commercial products.
Storage of commercial products.
Shipment of commercial products.
Supply of reagents, catalysts, lubricating oils.
Supply of compressed air, nitrogen and hydrogen.
Torch management.
Fuel supply system.
Laboratory control of production., Technological pipelines.
General plan of the plant.
Plant location. Situational plan.
Principles for constructing a master plan for refineries and petrochemical plants.
H. Engineering networks and technological pipelines.
Vertical layout. Drainage from the site.
Transport systems.
Improvement and landscaping of an industrial site.
Enterprise security.
Title list of enterprise objects.
Energy supply of the enterprise.
Heat supply.
Electricity supply.
Water supply.
Protection of the external environment from pollution by harmful emissions.
Oil refineries and petrochemical plants.
Sources of harmful emissions into the atmosphere.
Design solutions to reduce air pollution.
Wastewater, sources of its formation, characteristics, sewerage systems.
Calculation of maximum permissible and temporarily agreed upon emissions.
for refineries and petrochemical plants.
Development of installation and construction parts of the project.
Installation design.
Construction tasks.
Construction design.
The cost of construction is a feasibility study.
indicators.
Determination of the estimated cost of construction.
Technical and economic indicators of oil refineries and petrochemical plants.
Some issues of organizing the construction of oil refineries and petrochemical plants.
Construction methods.
Directorate of the enterprise under construction.
Capital construction planning.
Launch complex and launch passport.
Projects for organizing construction and work execution.
Providing refineries and petrochemical plants under construction with equipment and materials.
Capacity development within the required time frame.
| Title of the document | VUPP-86 Departmental guidelines for the design of industrial water supply, sewerage and wastewater treatment of oil refining and petrochemical industries |
| Start date | 01.07.1986 |
| Acceptance date | 14.04.1986 |
| Status | Active |
| To replace | VNTP 25-79 |
| Approval document | Order dated April 14, 1986 No. 356 |
| Document type | Directions |
| Document code | VUPP-86 |
| Developer | |
| Receiving authority | All-Union Research and Design Institute of Oil Refining and Petrochemical Industry (VNIPIneft) |
This document does not contain references to other regulatory documents.
Other normative documents do not refer to this document.
MINISTRY OF OIL REFINING AND PETROCHEMICAL INDUSTRY OF THE USSR
DEPARTMENTAL INSTRUCTIONS
FOR DESIGNING PRODUCTION WATER SUPPLY,
SEWERAGE AND WASTEWATER TREATMENT FOR OIL REFINING AND PETROCHEMICAL INDUSTRY ENTERPRISES
Moscow - 1986
1. GENERAL PROVISIONS
1.1. These “Departmental Instructions” were developed in pursuance of the Resolution of the Central Committee of the CPSU and the Council of Ministers of the USSR dated April 29, 1984 No. 387 “On improving the planning, organization and management of capital construction” (Order of the USSR Ministry of Petroleum and Chemical Industry dated June 4, 1984 No. 442), Resolution of the Council Ministers of the USSR dated January 28, 1985 No. 96 and order of the Ministry of Petroleum and Chemical Industry of the USSR dated February 23, 1985 No. 203 “On further improvement of design estimates and increasing the role of expertise and designer’s supervision in construction.”
1.2. “Departmental instructions” take into account the requirements of the “Instructions on the procedure for developing new and revising existing norms of technological design” with additions arising from the Decree of the USSR State Construction Committee No. 33 of March 24, 1980, and “Instructions on the composition, procedure for development, coordination and approval of design - estimate documentation for the construction of enterprises, buildings and structures" (SNiP 1.02.01-85).
1.3. “Departmental instructions” have been revised taking into account the implementation of scientific and technological achievements in projects, advanced technology, advanced equipment, and economical use of raw materials and energy resources.
1.4. “Departmental instructions” are linked to the requirements of current all-Union regulatory documents and instructions for design and construction, state standards, sanitary and fire safety standards, safety regulations and environmental protection standards.
water supply and sewerage networks, layout solutions for pumping stations, installation and piping of equipment, control and automation, mechanization of labor-intensive work, safety precautions, environmental protection.
1.5. “Departmental instructions” are mandatory for use when designing water supply, sewerage and wastewater treatment facilities for oil refineries and petrochemical plants located on the same site.
1.6. When designing water supply and sewerage systems for enterprises, it is necessary to introduce the most advanced technology for the preparation and supply of water, disposal and treatment of wastewater. The main task is to develop measures to sharply reduce the discharge of industrial wastewater, reduce production waste in order to create enterprises with minimal discharge of industrial wastewater into water bodies.
When choosing a technological scheme for an enterprise, progressive production technology should be used to ensure the least formation of contaminated wastewater and maximum use of waste process solutions.
1.7. When developing forecasts, feasibility studies, and choosing water supply and sewerage schemes for industrial hubs and economic administrative regions, water consumption and the amount of wastewater for oil refining and petrochemical enterprises should be taken according to the indicators given in the “Optimal Standards of Water Consumption and Wastewater Disposal”, published by VNII VODGEO and “Enlarged specific indicators” published by the USSR Ministry of Water Resources, as well as on enlarged long-term standards for water consumption and wastewater disposal at oil refining and petrochemical industry enterprises.
To draw up projects for oil refining and petrochemical enterprises, water and wastewater consumption should be taken according to the designs of technological installations, workshops and production facilities included in the enterprise being designed, taking into account the quality of processed oils and progressive indicators (achieved in modern installations.
1.8. When designing structures and networks of water supply and sewerage, the order of construction of the enterprise should be taken into account.
Each launch complex must include treatment facilities that ensure complete wastewater treatment and disposal of waste from facilities being put into operation.
1.9. When choosing sources and systems of water supply and sewerage, it is necessary to provide for the cooperation of enterprises of an industrial hub in the construction of water intakes, water treatment stations, main water pipelines, taking into account the regional planning project, the general scheme of water supply and sewerage, and schemes for the integrated use and protection of water resources.
1.10. The amount of waste water should be minimal. Wastewater discharged from individual installations and production into the enterprise's sewerage system must not contain contaminants that impede or complicate their treatment.
1.11. According to GOST 17.1.4.01-80 “Nature conservation. Hydrosphere. General requirements for methods for determining petroleum products in natural and waste waters” The term “petroleum products” includes non-polar and low-polar hydrocarbons (aliphatic, aromatic, alicyclic), which make up the main and most characteristic part of oil and its refined products.
The most accurate results for the determination of petroleum products can be obtained using the method of column chromatography with gravimetric or IR spectrophotometric termination.
1.12. In industries where wastewater is polluted with specific substances, local recycling and treatment plants should be provided as part of the production flow chart.
In places where wastewater is generated that is contaminated with a significant amount of petroleum products (draining and loading racks, raw material and commodity *parks, etc.), it is advisable to provide local structures that ensure the capture of the main amount of petroleum products.
1.13. The discharge of wastewater into water bodies is carried out in compliance with the conditions stipulated by the “Rules for the protection of surface waters from pollution by wastewater”, “Guidelines for the application of the rules for the protection of surface waters from pollution by wastewater”, “Rules for the protection of coastal waters of the seas from pollution”. When discharging industrial wastewater into the city sewerage system, discharge conditions must be provided in accordance with the “Rules for the acceptance of industrial wastewater into the sewerage systems of populated areas” of the Ministry of Housing and Communal Services of the RSFSR.
1.14. For new technological processes, the method of wastewater treatment is adopted according to the technological regulations of the research institute.
1.15. In order to prevent contamination of groundwater and adjacent lands, all earthen structures must be non-filtering. Depending on the external conditions, protective measures and control over the quality of groundwater in the area of these structures should be provided.
Note. Developments of insulation of earthen structures are carried out according to the recommendations of research institutes.
1.16. Enterprises must organize constant monitoring of the operation of water supply and sewerage facilities, the quality of water and wastewater in accordance with the “Safety Rules” PTB NP, second edition, “Standard instructions for the operation of water supply and sewerage systems in the oil refining and petrochemical industry” (Approved by VPO Soyuznefteorgsintez ").
To ensure control of circulating water supply systems and treatment facilities, it is necessary to provide flow metering devices in the schemes, which should be located:
On the main pipelines of circulating water supply systems;
On make-up water pipelines;
In places where process wastewater is generated before discharging it into the appropriate sewerage systems;
At general plant treatment facilities.
1.17. Production laboratory monitoring of the efficiency of treatment facilities should be carried out according to the “Methodological Guide for the Analysis of Wastewater from Refineries and Petrochemical Plants”, second edition, approved by the USSR Ministry of Petrochemical Industry, agreed with the USSR Ministry of Health and the USSR Ministry of Water Resources, according to OST 38.01195-80 “Technical, recycled, waste water - oil refineries. Methods for determining suspended and dissolved substances”, as well as PG 601-23-83 “Nature conservation. Hydrosphere IR - a spectrophotometric method for determining the content of petroleum products in wastewater."
When using domestic wastewater, production laboratory control should be carried out according to the “Methodological instructions for the hygienic assessment of the use of post-treated municipal wastewater in industrial water supply”, 1985.
1.18. When designing, it is necessary to provide for the use of standard designs of buildings and structures. The use of individual projects is allowed only in the absence of standard projects and in special cases with appropriate justification.
1.19. When designing water supply and sewerage systems, it is necessary to ensure the maximum possible blocking of structures: pumping stations with electrical substations, filtration stations with reagent facilities, nitrogen tanks with settling tanks, etc., as well as the enlargement of units, cooling towers and other equipment.
When choosing cooling towers, pumps and other equipment, it is necessary to take into account the provision of water consumption during construction phases and the possibility of shutdowns for repairs.
1.20. Pumping units for circulating water supply should be designed non-buried with pumping units located above the ground surface.
Note. If it is impossible to design non-buried pumping stations, it is permitted, with appropriate justification provided in the project, to design buried pumping stations for circulating water supply.
1.20.1. Place the pumps 1 m below the minimum water level in the tank or chamber.
1.20.2. Provide measures to ensure reliable protection of pumping stations from flooding.
1.20.3. For buried pumping stations, measures should be taken against flooding of pumping units:
a) in case of an accident outside the building
Appropriate design of the building and layout around the pump house;
b) in case of an accident inside the building
Gravity sewerage, taking measures against flooding of the pumping station during backwater in the sewer network during rains;
In case of limited capacity of gravity sewerage or impossibility (connection to it from the level of the turbine hall floor, except for a pump for pumping out drainage water), install a special vertical pump with an hourly capacity equal to approximately the volume of the buried part of the turbine hall with a height of one meter.
The electric motor of the specified pump should be located above the planning level of the pumping house building, and it should be started automatically depending on the water level in the turbine room;
Possibility of pumping water with two hot or chilled water pumps.
1.21. Suction and pressure pipelines in pumping stations should be laid above the floor surface with bridges installed over the pipelines and access to units and valves provided. U (laying pipes in basements and trays is not allowed.
1.22. Pumping stations buried more than 0.5 m must be equipped with gas analyzers with automatic alarms.
If there is a threat of gas contamination in the pumping room, emergency ventilation is switched on.
1.23. On a site with mild climatic conditions (GOST 15150-69 “Machines, instruments and other technical products. Design for various climatic regions”) and with short winters, pumping stations should be designed under canopies, similar to technological ones, providing for floor heating and appropriate measures against freezing pipelines and fittings.
1.24. To operate equipment, fittings and pipelines in pumping stations, mobile floor lifting equipment or stationary overhead cranes, monorails, as well as passages for electric forklifts and trolleys should be used. Lifting devices must provide the ability to load pumps and individual components onto mobile vehicles. The length of the supporting beams of overhead cranes should be selected taking into account the area of dismantling and installation work in the pump room.
1.25. When extinguishing a fire, it is allowed to use water from circulating water supply systems to cool technological equipment.
1.26. The capacity of the industrial wastewater network must be additionally designed to accept 50% of the fire water flow, if 50% of the fire flow is greater than the calculated rain flow entering the sewer system.
1.27. When calculating networks and structures of water supply, sewerage and treatment facilities, one should take into account the possibility of forced operation of promising technological installations up to 20%.
1.28. The design of water supply and sewerage networks must be carried out taking into account and coordination with engineering networks for other purposes.
Industrial water supply pressure networks must be circular. Pressure pipelines from pumping stations to ring networks must be laid in at least two threads, the second thread being a reserve one or each thread for the calculated water flow. The number of inputs per installation is determined based on the technological need for the layout of the heat exchange equipment and the flow of circulating water,
1.29. Pressure pipelines for water supply and sewerage, as a rule, should be located on low and high supports and overpasses together with process and heating pipelines. If necessary, it is possible to independently install pressure industrial water pipelines and sewerage collectors.
1.29.1. Steel pipes should be used for pressure water supply, sewer and water pipelines laid throughout the enterprise territory. On networks laid above the ground surface, it is necessary to use steel reinforcement.
1.29.2 Control of valves and gates installed in wells must be carried out from the surface of the ground:
with manual drive for DN 50-400 mm, with electric drive for DN over 400 mm. Electrically operated valves must also be controlled remotely.
1.30. When laying underground pressure networks of industrial water supply systems, the installation of diaphragms or other* measuring elements should be carried out on sections of pipelines brought to the surface of the earth.
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Range of services provided in the field of refinery design
The professional activities of our organization cover a wide area of designing all kinds of objects, including the design of oil refineries. The information specified in the application is the basis for creating a refinery project, which can be represented by a standard, complex or non-standard structure. The services provided by our organization include the following:
Our responsibilities in terms of general design. We are entrusted with the responsibility for creating and conducting all necessary approvals regarding the project, including the processes of field supervision, but at the same time, the processes of manufacturing and assembling the refinery are carried out by another organization.
The process of developing individual fragments of a set of construction documentation. Here the necessary sections of the project are being studied, examples of which can be: KM - metal structures; KMD – metal detailing structures; KZh – reinforced concrete structures.
General contracting function. The general contracting position involves the general contractor performing certain tasks in both design, installation and production matters, including the procedure for obtaining all approved approvals and documents allowing the commissioning of the specified refineries.
The client does not incur material costs when providing preliminary assessment services for the declared project, calculating the estimated cost and estimated time frame for the execution of these works in our organization. If you have any questions, you can contact our employees to receive complete and detailed information.
To submit an application for the execution of the design of an oil refinery, as well as the implementation of work within the framework of a general contract, is carried out using the methods proposed below:
- Fill out an application online on the organization’s website
In the submitted application form, fields with mandatory contact information are filled in. In turn, available project documents are attached as an attached file. Materials can have different volumes, which depend on the specific tasks set by the customer. We guarantee compliance with confidentiality rules regarding all information transmitted to us. If you have documents related to the project, you place them at our disposal. In the absence of design documentation, it is necessary to provide a description of the refinery and indicate the required characteristics of its buildings. When the information provided is insufficient, a representative of our organization will call you back to supplement and clarify the data. - Via telephone connection
It is a popular and efficient method of communication, the possibility of which consists in a two-way discussion of information regarding the composition of the project and the required work. Our employee will answer all your questions and offer alternative solutions that will allow you to reduce the price of services as much as possible. - Visiting the organization's office in person Your visit to us will give you the opportunity to personally familiarize yourself with the activities of our organization and evaluate its capabilities, as well as discuss all the nuances of the project directly on the spot.
The customer can provide the design information in a suitable and convenient form, for example, printed on paper or use electronic media (USB drive, attach a file to an email, etc.).
If you filled out an application on our organization’s website or submitted it via email, you will be informed of its receipt as soon as possible.
- Independent performance of services and works provided
Having a sufficient number of specialists on our staff, our organization provides a comprehensive work process and also has all the necessary equipment and technologies. We have capabilities that allow us not to resort to the services of subcontracting companies. Due to the fact that third parties and organizations are not involved in the design work, it is completed in a shorter time frame. In addition, it is convenient for the customer, since the order is made in one place. - The quality of work is excellent
Our organization’s use of the most advanced software systems contributes to the high quality of work, which also allows us to reduce time costs. - Availability of a large staff of specialists
The personnel of our organization is represented by an extensive professional staff and a stable staff of employees who are able to ensure timely and high-quality completion of all assigned tasks. Having at our disposal specialists in all the necessary specialized areas, we provide guaranteed performance of work of the appropriate level. - Many years of experience
At the moment, we are among the top companies that lead the design services market. Over the period of many years of work, our organization has implemented a sufficient number of refinery projects. The experience gained over many years of activity is one of the significant factors guaranteeing a high level of quality and timeliness of the work performed. - Carrying out control processes for quality work performance
We have developed a multi-stage quality control system covering all types of work. Representatives of the quality control department regularly inspect the project, which contributes to the timely identification and resolution of emerging problems from the first steps. - Minimum terms
Thanks to our extensive long-term experience in the field of designing oil refineries, we have the opportunity to minimize the time required for carrying out the necessary work. In addition to the high level of skill of our employees, the use of the latest technologies helps reduce time costs. - Reviews and recommendations
Our organization has a large number of clients who contacted us and were satisfied with the quality of the work performed. This confirms the list of positive recommendations. If you would like to see the list of recommendations and the companies that provided them, you can do this by going to our website in the appropriate section. Additional information can be obtained by contacting representatives of our company.
Significant indicators that can influence the determination of the timing of the design of oil refineries are the complexity of the structure configuration and the upcoming scope of design. The components of the documentation submitted for development influence the duration of the refinery design. Deadlines are set for each object on an individual basis. After determining the deadlines, a representative of our organization offers a commercial proposal, which is accompanied by a detailed schedule of the schedule in a graphical image. It contains information about the periods of work carried out for each specific part of the project and their payment. Mostly, the starting stage of design is tied precisely to the moment of payment of the advance payment; these conditions are specified in the contract.
Our organization carries out refinery design within the minimum deadline, but not less than 3 days. For simple projects, evaluating a project assignment submitted to us takes no more than 15 minutes. Evaluating projects with increased complexity or degree of uniqueness involves a longer process.
Accordingly, individual settlement operations are carried out for each project, the value of the indicators varies depending on various factors. The evaluation criteria are the composition of the required design work, the need for production work and the installation process. The complexity of the project and the workload of the department during the order period are taken into account.
- Simple objects
Typical refinery structures with high repeatability (for example, hangars) have this design structure. They are objects with a simple and labor-intensive structure. These structures are characterized by many rolled-profile trusses, which alternate each other and have the same dimensions, and can also be represented by welded beams of variable cross-section. - Complex objects
Almost all refinery facilities can be included in this category, since many industrial buildings are regarded as complex. Their peculiarity is the presence of a huge number of drawings and labor costs. The defining quality of complex objects is the low repeatability of elements or the absence of repeatability at all, which constitutes a certain labor intensity, both in design and in production and installation work. - Unique objects
The uniqueness of the refinery facilities is the complex geometric configuration of the walls and roofs. Their designs are quite complex structures.
With all this, there is no clear line in delimiting the above price categories, due to the fact that even an elementary simple project may have special requirements. This may relate to the specifics of documentation and the need for certain additional work, which increases the overall cost of the project. Also, in addition to complexity, it is necessary to take into account such factors as the lack of repeatability of refinery designs. This leads to the fact that at the design stage, labor costs increase, the complexity of the manufacturing and installation processes increases. Based on the presence of such specifics, the establishment of prices for each project is based on individual approach.
Initial information makes it possible to determine the level of project readiness.
These materials can be provided in any form convenient for the customer. So, the application may look like this:
- Verbal description
In fact, if the design of a refinery is at an early stage or the customer does not yet have a clear idea of its design features, he does not have sets of completed drawings. In this case, he can express his thoughts and wishes orally. And while in the office, you can discuss the main key points of cooperation and the main constructive decisions. This presupposes the possibility of determining and clarifying the parameters of the object and considering the main steps for the implementation of the project. Thus, after oral study, you can create a high-quality assignment for design work. - Text presentation
The description of the list of basic requirements for the object comes down to drawing up a design assignment. It is necessary to indicate the desired dimensions and standard plans of the refinery, as well as attach a text description of the required design solutions. If the design task is formulated correctly and efficiently, then its basis can be the basis for the development of architectural drawings. - Package of drawing documentation
As a resource of source materials, sets of drawings can be offered: for architectural solutions - AR, or for architectural and construction solutions - AC. They allow calculations of building layouts and bearing capacity of refinery structures. Based on the provided set of drawings, a set of CM drawings is developed.
A set of drawings for metal structures (MS) is subject to mandatory expert evaluation. Having received approval, you can begin developing KMD - a set of drawings for metal detailing structures. The package of this documentation will be required in the future directly for production by the manufacturer.
The contract specifies the payment procedure between the design organization and the customer. The regulations of the contract stipulate all stages of payment regarding the work performed, their types and volumes. An approximate payment scheme could look like this:
- First, a payment must be received into the account of our organization. Its payment is a condition for starting the design of the refinery. As a rule, this amount is small, its size is limited to 20-30% of the full price.
- Start of design work. This stage involves the implementation of the main tasks of designing a refinery by our engineers.
- Interim delivery of the project is carried out in stages and depends on various factors, including the volume of the order. This is determined by the contract, which specifies the recommended number of issues. For example, for small refinery structures this type of delivery is not planned in principle.
- Interim payment. It is tied to intermediate issues, and specifically, each such issue is followed by a corresponding payment.
- Expertise is also often correlated with payments. The results of the expert study of the project determine whether amendments are required to it. If no errors are found, the project does not need to be amended, and therefore the deadline for completing the order will not be changed.
- Lack of installation diagrams when issuing the project. This step is due to the fact that we have a guarantee that funds will be received for the work done in full and on time.
- The final payment is the final stage of our interaction with the customer. Its final point is the procedure for signing the certificate of completion of work and, accordingly, payment.
The given payment scheme for services may differ due to possible differences in the presented projects. Depending on the volume of work that will be carried out, some items may be omitted or new ones may be added. Features of the work are present when interacting with foreign clients. For example, the calculation of the amount of payment for work performed as a whole is based on the cost of 1 working hour.
A certain design object is characterized by the presence of several stages of the life cycle, however, some of the stages are applied only to objects subject to expert analysis.
The stages of the life cycle of an oil refinery can be represented in the following regulations:
- Design Process
- Carrying out approval activities
- Construction work
- Commissioning of the refinery facility
Most customers put forward requests for completely finished refinery buildings with a clear requirement for operational characteristics (area, number of floors, etc.). What is important to the client is the result at a minimum price and high efficiency of use of the facility. But such issues as design features, complexity, the essence of design and manufacturing, and the cost of installation work, as a rule, are not of great interest to him.
In order to make it easier for you to determine the most suitable option in a combination of design characteristics, materials and technologies for creating a refinery, our organization can offer you a free consultation. Our leading engineer will provide you with a consultation providing comprehensive and competent information about the positive and negative aspects of each individual design solution. With its help, you can make the most rational choice. To determine a suitable structural scheme, there is a need to carry out simultaneous calculations of a certain number of such schemes based on different solutions. An example of this approach is the choice of floors for a refinery, since there are several types of them: based on rolled beams, welded beams of variable cross-section and thin-walled elements. The problem of choice is that without carrying out a calculation it is not possible to determine which option will be the most economically justified for a particular project. For this purpose, three schemes are calculated at once, which helps achieve about 5% savings, and this figure is quite significant, considering the price of the entire project.
Carrying out this kind of calculations is an extremely important stage in the design of a refinery, where the safety of its operation is determined by the correctness and accuracy of the calculation actions. Their essence lies in the error-free calculation of the load that each detail of the refinery structure will bear. This will make it possible to make a clear selection of the cross-section for such a load, subject to all relevant standards adopted in the Russian Federation. The calculations are influenced by such a significant factor as the specific location of the refinery. They affect the calculation of loads, since it is impossible not to take into account atmospheric influences, frequency and level of precipitation, and seismicity.
Structural calculations of a refinery are based on the following stages:
- strength calculation By calculating this indicator, we will find the value of the load force to which each individual structural part will succumb, and in accordance with these data, the required section will be selected.
- stiffness calculation The value of this indicator determines the level of maximum displacement, or deformation. All probable movements are checked to determine whether the refinery structures maintain the required operational characteristics.
- stability calculation Stability parameters can be lost much earlier than the strength coefficient. Of paramount importance here is an absolutely accurate calculation of the stability of future refinery structures.
- node calculations The calculations are carried out during the development of the CM, and are refined at the stage of creating the MDC (metal detailing structures).
- calculation of progressive destruction This involves monitoring the impact of sudden failure on refinery structures. To carry out such a calculation, by excluding one part, a sharp destruction of a specific structural element is simulated - columns, beams, etc. When a structure is destroyed when one of its parts is removed, the only solution in this case is a complete recalculation of the project.
Qualified specialists of our organization are able to calculate any refinery designs, regardless of their level of complexity. Calculation operations and actions for each project are carried out on the basis of two software packages, the results of which are then verified. These results should be almost identical, with only minor differences acceptable.
By visiting our organization’s website, you can find information about many projects developed by our engineers. The calculations are based on programs such as SCAD and RobotStructuralAnalysis. If there is a need to familiarize yourself with a more complete list of refinery projects calculated by us, you can obtain such information either by calling us or by visiting our company office.
The customer receives the design documentation in printed form or in electronic form. The contract establishes the number of printed copies. The electronic format for storing information can be offered on Flash drives or CDs - the option is agreed upon in advance according to the customer’s wishes.
Among the most commonly used types of project delivery are:
- DXF is universal and therefore popular among customers due to the ability to save not only standard drawings in one plane, but also 3D layouts.
- DWG is common for engineering programs. Using AutoCAD and Autodesk formats, two- and three-dimensional projections of drawings can be saved.
- IFC is a special IndustryFoundationClasses file format designed to provide data exchange and consistency between specific programs. This version is free, as it does not have a specific copyright holder.
- PDF is one of the most common Adobe formats due to the ability to quickly and conveniently view any type of material - text, tables, drawings, 3D projections. A formatted file with a large number of pages is not difficult to print.
The electronic version of the project transfer must contain drawings, explanations, as well as a 3D model of the refinery. When the customer intends to independently build an oil refinery, then NC (LSTV) files are issued to control numerically controlled machines.
Control accompanies all stages of refinery design, without exception, to guarantee the quality of documentation and the implementation of further manufacturing and installation processes. Our organization carries out the following mandatory levels of control:
- Development engineer review is a significant process in which materials are subjected to careful review by a specialist. If errors are found, the engineer corrects them immediately. At this stage, qualified workers will cancel most of the shortcomings. We use a method of mutual verification of engineers working on the project. This helps to avoid mistakes during the work process.
- Regulatory control. Engineers check the compliance of the design documentation with the established quality standards for the design and manufacture of refineries, prepared by the design department. This stage involves correcting the design and content to eliminate errors. This work does not concern design solutions, but is aimed only at ensuring that the design meets the requirements.
- Control functions of the chief project engineer. The leading engineer, being legally responsible to the customer, shows interest in ensuring a high-quality result of work at the first stage, that is, design, even before the customer receives the project. The chief engineer is responsible for coordinating and approving absolutely all design solutions for the project.
- Automatic control of the software package. The progressive programs used in the work, which speed up and facilitate the work on designing a refinery in an automatic way, help to avoid errors in quality control. They are programmed so that incorrect data is not issued or omitted. Therefore, projects developed through the use of such programs serve as a guarantee of the accuracy of refinery installations.
- Architectural supervision, installation supervision. Highly qualified engineers provide quality control to various levels of work performed, such as design, manufacturing, construction, and commissioning of the developed project. Such control is the key to a high degree of reliability and quality of manufactured oil refineries.
At the request of the customer, the competent employees of our organization can perform many types of refinery quality control, such as non-destructive testing.
In the process of cooperation, an already created, ready-made project can be an option for a design solution. Such solutions are systematized in our catalogs. The necessary amendments are made to each completed project in accordance with the customer’s requirements for the future refinery. The adjustment process does not seem to be as labor-intensive in comparison with the initial formation of project documentation and has a reduced time frame for completing all work. This type of cooperation between the customer and the contractor can also bring economic benefits, as it can reduce financial costs by more than 50%.
The impressive volume of completed orders and developments in this area gave us the opportunity to compile a catalog of examples of refineries.
Typical designs can be classified into the following types:
- Truss roof structures
Such structures are often used in production, so with a high probability it can be said that choosing suitable options from the catalog will be quite simple. Truss structures can have various configurations from a square or round pipe, or from paired corners. - Structures, the roof configuration of which is represented by welded beams with variable cross-section
It is also a common one, so in our list you can choose one that matches your request. - Designs based on the use of thin-walled elements
The creation of thin-walled elements involves the use of a minimum volume of metal raw materials. A thin-walled structure can be a structure made with a rolled wall thickness of 2-4 mm. With low metal consumption, this material is characterized by savings, which implies increased demand. Similar designs are suitable for creating low-rise buildings. - Tent structures
These structures are characterized by a roof with a non-solid type of covering, often represented by polymer materials. Tent structures serve as temporary shelters or unheated rooms.
If you have any difficulties choosing the type of design, you can contact our staff. They will provide explanations about the positive and negative aspects of each design type, outline the details, and assist in choosing an option that will more closely match the request.
Since on the website we have indicated only the main examples, classified according to the design specifics, the full scope of the projects we have produced can be found in the management department of our specialists. The refinery samples presented here were developed on the basis of advanced three-dimensional modeling techniques.
Technologies for designing metal structures are in a constant dynamic of development. We set ourselves the task of continuously improving the quality of refinery design, introducing all kinds of innovations into work, and at the same time striving to improve the methods and skills already mastered by our designers. Continuous development is important to us, so studying developments from all over the world and translating them into our production process is one of our main tasks. Our organization has established a training process to expand the qualifications of personnel, study and implement world practices in the field of modernized developments. Operating with modern technological programs helps to achieve automation of the work cycle, and eliminates the increased labor intensity of the designer’s work, which is associated with the calculations of various types of statements and the preparation of reports.
Not so long ago, the execution of maps for cutting sheet and rolled profiles was carried out by hand, which implied a high labor intensity of execution. Today, automatic support is used to facilitate this type of work.
- Definition of routing
This is a documentary statement for the production of a refinery, which is generated under the conditions of in-plant document flow. Having an asset of software systems that meet all modern requirements. For our organization, drawing up such a map according to the declared type is a matter of several minutes. - Sheet profile cutting chart
Its contents are diagrams that detail how it is necessary to correctly “cut” all the component parts onto prepared sheets so that the waste amounts to very little. The program itself scans hundreds of options for how parts should be placed on the sheet, and selects the most optimal option from among them. So at the end you can save materials with savings of 5-7%. This card is a task for cutting using the plasma cutting method. - Rolled profile cutting chart
She has information on how to place rolled steel parts on a twelve-meter canvas. Its use significantly saves material. Our organization carries out cards for cutting rolled profiles at an automatic level, so this service is free. The basis for creating such maps involves an error-free calculation of the percentage of cutting and makes it possible to estimate the final cost of the project for the production of a product. To do this, you need to enter data such as the weight of the project and the cutting percentage.
The process of assembling and installing a refinery is almost always a complex procedure. Our organization is ready to take on the responsibilities of conducting design supervision, examination and project support from specialized specialists for the entire construction period. The service implies that the engineer responsible for the refinery project is personally present during installation. The person responsible for the author's supervision carries out control operations that require maintaining correct and consistent work schedule for the installation of the refinery. The approximate time a representative will spend at a given site is 1-2 weeks. If there is an agreement with the client to establish a different time period, the organization’s employees are at each stage, which implies a better guarantee of the quality of the product.
When concluding an agreement, the parties immediately establish payment criteria and the period of work of the field supervision specialists accompanying the project during construction.
The organization designs a refinery and provides a full package of services, the final stage of which is the commissioning of the finished product. Our company's employees in various fields have extensive experience in implementing refinery projects. To warn against dubious related enterprises and save time, we recommend that you order design, manufacturing and installation work from our organization. We have all the components for this: modern machines, many implemented projects, practical production location - near Moscow.
The organization has at its disposal an installation department and a team of specialists to carry out installation work. The specialists of our organization are responsible for the high quality of work performed at any stage of refinery manufacturing, the same applies to the construction site.
To carry out the tasks of designing a refinery, the enterprise must be part of an SRO - a self-regulatory organization. Our membership in the SRO lasts for more than six years. We provide supporting documentation to the client either via email or the original in the office.
Preparation of design documentation developed outside the Russian Federation, and without compliance with Russian standards and rules, is subject to complex examination. Design documentation generated by foreign specialists requires redesign. Everything must be adapted to the existing standards of the Russian Federation “from scratch”: relevant documentation, calculations, drawings, calculation of loads on the entire structure of the refinery. These operations for processing source documentation are design. The execution of design takes a significant proportion of time compared to redesign, since the approval and adoption of most design decisions and issues has already taken place.
The circumstance causing the need for redesign also lies in the need to adapt part of the KMk to the regulated parameters of Russian legislation, since the original form may contain erroneous data on the tonnage of the structure and the design decisions taken. In this case, redesign is an opportunity to reduce the weight of the structure and save financial costs.
Full name: LLC "INSTITUTE FOR DESIGNING ENTERPRISES OF OIL REFINING AND PETROCHEMICAL INDUSTRY"
Taxpayer Identification Number: 7810327462
Type of activity (according to OKVED): 71.11 - Activities in the field of architecture
Type of ownership: 16 - Private property
Organizational and legal form: 12165 - Limited liability companies
Reporting prepared in thousand rubles
See detailed verification of the counterparty
Accounting statements for 2011-2017.
1. Balance sheet
| Indicator name | Code | #DATE# |
|---|---|---|
| ASSETS | ||
| I. NON-CURRENT ASSETS | ||
| Intangible assets | 1110 | #1110# |
| Research and development results | 1120 | #1120# |
| Intangible search assets | 1130 | #1130# |
| Material prospecting assets | 1140 | #1140# |
| Fixed assets | 1150 | #1150# |
| Profitable investments in material assets | 1160 | #1160# |
| Financial investments | 1170 | #1170# |
| Deferred tax assets | 1180 | #1180# |
| Other noncurrent assets | 1190 | #1190# |
| Total for Section I | 1100 | #1100# |
| II. CURRENT ASSETS | ||
| Reserves | 1210 | #1210# |
| Value added tax on purchased assets | 1220 | #1220# |
| Accounts receivable | 1230 | #1230# |
| Financial investments (excluding cash equivalents) | 1240 | #1240# |
| Cash and cash equivalents | 1250 | #1250# |
| Other current assets | 1260 | #1260# |
| Total for Section II | 1200 | #1200# |
| BALANCE | 1600 | #1600# |
| PASSIVE | ||
| III. CAPITAL AND RESERVES | ||
| Authorized capital (share capital, authorized capital, contributions of partners) | 1310 | #1310# |
| Own shares purchased from shareholders | 1320 | #1320# |
| Revaluation of non-current assets | 1340 | #1340# |
| Additional capital (without revaluation) | 1350 | #1350# |
| Reserve capital | 1360 | #1360# |
| Retained earnings (uncovered loss) | 1370 | #1370# |
| Total for Section III | 1300 | #1300# |
| IV. LONG TERM DUTIES | ||
| Borrowed funds | 1410 | #1410# |
| Deferred tax liabilities | 1420 | #1420# |
| Estimated liabilities | 1430 | #1430# |
| Other obligations | 1450 | #1450# |
| Total for Section IV | 1400 | #1400# |
| V. SHORT-TERM LIABILITIES | ||
| Borrowed funds | 1510 | #1510# |
| Accounts payable | 1520 | #1520# |
| revenue of the future periods | 1530 | #1530# |
| Estimated liabilities | 1540 | #1540# |
| Other obligations | 1550 | #1550# |
| Total for Section V | 1500 | #1500# |
| BALANCE | 1700 | #1700# |
Brief balance sheet analysis
Chart of changes in non-current assets, total assets and capital and reserves by year
| Financial indicator | 31.12.2011 | 31.12.2012 | 31.12.2013 | 31.12.2014 | 31.12.2015 | 31.12.2016 | 31.12.2017 |
|---|---|---|---|---|---|---|---|
| Net assets | 1734973 | 1670644 | 1474575 | 1248968 | 1235150 | 1277235 | 1250946 |
| Autonomy coefficient (norm: 0.5 or more) | 0.88 | 0.6 | 0.64 | 0.61 | 0.69 | 0.65 | 0.71 |
| Current liquidity ratio (norm: 1.5-2 and above) | 9.7 | 4.7 | 6.1 | 3.9 | 5 | 3.7 | 4.9 |
2. Profit and loss statement
| Indicator name | Code | #PERIOD# |
|---|---|---|
| Revenue | 2110 | #2110# |
| Cost of sales | 2120 | #2120# |
| Gross profit (loss) | 2100 | #2100# |
| Business expenses | 2210 | #2210# |
| Administrative expenses | 2220 | #2220# |
| Profit (loss) from sales | 2200 | #2200# |
| Income from participation in other organizations | 2310 | #2310# |
| Interest receivable | 2320 | #2320# |
| Percentage to be paid | 2330 | #2330# |
| Other income | 2340 | #2340# |
| other expenses | 2350 | #2350# |
| Profit (loss) before tax | 2300 | #2300# |
| Current income tax | 2410 | #2410# |
| incl. permanent tax liabilities (assets) | 2421 | #2421# |
| Change in deferred tax liabilities | 2430 | #2430# |
| Change in deferred tax assets | 2450 | #2450# |
| Other | 2460 | #2460# |
| Net income (loss) | 2400 | #2400# |
| FOR REFERENCE | ||
| Result from the revaluation of non-current assets, not included in the net profit (loss) of the period | 2510 | #2510# |
| Result from other operations not included in the net profit (loss) of the period | 2520 | #2520# |
| Total financial result of the period | 2500 | #2500# |
Brief analysis of financial results
Graph of changes in revenue and net profit by year
| Financial indicator | 2012 | 2013 | 2014 | 2015 | 2016 | 2017 |
|---|---|---|---|---|---|---|
| EBIT | 306194 | 272150 | 345625 | 238348 | 271957 | 223938 |
| Return on sales (profit from sales in each ruble of revenue) | 19.7% | 15.6% | 16.3% | 11.9% | 14.6% | 10.9% |
| Return on equity (ROE) | 14% | 14% | 20% | 15% | 17% | 14% |
| Return on assets (ROA) | 10.1% | 8.4% | 12.6% | 9.7% | 11.4% | 9.4% |
4. Cash flow statement
| Indicator name | Code | #PERIOD# |
|---|---|---|
| Cash flows from current operations | ||
| Receipts - total | 4110 | #4110# |
| including: from the sale of products, goods, works and services |
4111 | #4111# |
| lease payments, license fees, royalties, commissions and other similar payments | 4112 | #4112# |
| from resale of financial investments | 4113 | #4113# |
| other supply | 4119 | #4119# |
| Payments - total | 4120 | #4120# |
| including: to suppliers (contractors) for raw materials, materials, works, services |
4121 | #4121# |
| in connection with the remuneration of employees | 4122 | #4122# |
| interest on debt obligations | 4123 | #4123# |
| corporate income tax | 4124 | #4124# |
| other payments | 4129 | #4129# |
| Balance of cash flows from current operations | 4100 | #4100# |
| Cash flows from investment operations | ||
| Receipts - total | 4210 | #4210# |
| including: from the sale of non-current assets (except financial investments) |
4211 | #4211# |
| from the sale of shares of other organizations (participatory interests) | 4212 | #4212# |
| from the return of loans provided, from the sale of debt securities (rights to claim funds against other persons) | 4213 | #4213# |
| dividends, interest on debt financial investments and similar income from equity participation in other organizations | 4214 | #4214# |
| other supply | 4219 | #4219# |
| Payments - total | 4220 | #4220# |
| including: in connection with the acquisition, creation, modernization, reconstruction and preparation for use of non-current assets |
4221 | #4221# |
| in connection with the acquisition of shares of other organizations (participatory interests) | 4222 | #4222# |
| in connection with the acquisition of debt securities (rights to claim funds against other persons), provision of loans to other persons | 4223 | #4223# |
| interest on debt obligations included in the cost of an investment asset | 4224 | #4224# |
| other payments | 4229 | #4229# |
| Balance of cash flows from investment operations | 4200 | #4200# |
| Cash flows from financial transactions | ||
| Receipts - total | 4310 | #4310# |
| including: obtaining credits and loans |
4311 | #4311# |
| cash deposits of owners (participants) | 4312 | #4312# |
| from issuing shares, increasing participation shares | 4313 | #4313# |
| from the issue of bonds, bills and other debt securities, etc. | 4314 | #4314# |
| other supply | 4319 | #4319# |
| Payments - total | 4320 | #4320# |
| including: owners (participants) in connection with the repurchase of shares (participatory interests) of the organization from them or their withdrawal from the membership of participants |
4321 | #4321# |
| for payment of dividends and other payments | 4322 | #4322# |
| on the distribution of profits in favor of owners (participants) in connection with the repayment (redemption) of bills and other debt securities, repayment of loans and borrowings | 4323 | #4323# |
| other payments | 4329 | #4329# |
| Balance of cash flows from financial transactions | 4300 | #4300# |
| Balance of cash flows for the reporting period | 4400 | #4400# |
| Balance of cash and cash equivalents at the beginning of the reporting period | 4450 | #4450# |
| Balance of cash and cash equivalents at the end of the reporting period | 4500 | #4500# |
| The magnitude of the impact of changes in foreign currency exchange rates against the ruble | 4490 | #4490# |
6. Report on the intended use of funds
| Indicator name | Code | #PERIOD# |
|---|---|---|
| Balance of funds at the beginning of the reporting year | 6100 | #6100# |
| Funds received | ||
| Entry fees | 6210 | #6210# |
| Membership fee | 6215 | #6215# |
| Targeted contributions | 6220 | #6220# |
| Voluntary property contributions and donations | 6230 | #6230# |
| Profit from the organization's income-generating activities | 6240 | #6240# |
| Others | 6250 | #6250# |
| Total funds received | 6200 | #6200# |
| Funds used | ||
| Expenses for targeted activities | 6310 | #6310# |
| including: | ||
| social and charitable assistance | 6311 | #6311# |
| holding conferences, meetings, seminars, etc. | 6312 | #6312# |
| other events | 6313 | #6313# |
| Expenses for maintaining the management staff | 6320 | #6320# |
| including: | ||
| expenses related to wages (including accruals) | 6321 | #6321# |
| non-wage payments | 6322 | #6322# |
| expenses for official travel and business trips | 6323 | #6323# |
| maintenance of premises, buildings, vehicles and other property (except for repairs) | 6324 | #6324# |
| repair of fixed assets and other property | 6325 | #6325# |
| other | 6326 | #6326# |
| Acquisition of fixed assets, inventory and other property | 6330 | #6330# |
| Others | 6350 | #6350# |
| Total funds used | 6300 | #6300# |
| Balance of funds at the end of the reporting year | 6400 | #6400# |
2017 2016 2015 2014 2013 2012
No data for this period
| Indicator name | Code | Authorized capital | Own shares, purchased from shareholders |
Extra capital | Reserve capital | retained earnings (uncovered loss) |
Total |
|---|---|---|---|---|---|---|---|
| The amount of capital per | 3200 | ||||||
| Behind Capital increase - total: |
3310 | ||||||
| including: net profit |
3311 | X | X | X | X | ||
| property revaluation | 3312 | X | X | X | |||
| income attributable directly to capital increase | 3313 | X | X | X | |||
| additional issue of shares | 3314 | X | X | ||||
| increase in the par value of shares | 3315 | X | X | ||||
| 3316 | |||||||
| Reduction of capital - total: | 3320 | ||||||
| including: lesion |
3321 | X | X | X | X | ||
| property revaluation | 3322 | X | X | X | |||
| expenses directly attributable to reduction of capital | 3323 | X | X | X | |||
| reduction in the par value of shares | 3324 | X | |||||
| reduction in the number of shares | 3325 | X | |||||
| reorganization of a legal entity | 3326 | ||||||
| dividends | 3327 | X | X | X | X | ||
| Change in additional capital | 3330 | X | X | X | |||
| Change in reserve capital | 3340 | X | X | X | X | ||
| The amount of capital per | 3300 |
Additional checks
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* Indicators that are adjusted in comparison with Rosstat data are marked with an asterisk. The adjustment is necessary to eliminate obvious formal inconsistencies in reporting indicators (discrepancy between the sum of lines and the total value, typos) and is carried out according to an algorithm specially developed by us.
Reference: The financial statements are presented according to Rosstat data disclosed in accordance with the legislation of the Russian Federation. The accuracy of the data provided depends on the accuracy of the data submission to Rosstat and the processing of this data by the statistical agency. When using this reporting, we strongly recommend that you check the figures with the data of a paper (electronic) copy of the reporting posted on the official website of the organization or obtained from the organization itself. Financial analysis of the presented data is not part of Rosstat information and was performed using specialized
