QUESTIONS ASKED

1. What functional responsibilities will be added when the rank increases?

According to ETKS upgradable category.

2. What is AGZU and what is it intended for?

AGZU - automated group metering unit.

Designed to measure liquid flow rate (measure the flow rate of each well) and to measure pressure in the reservoir.

AGZU is designed to automatically record the amount of liquid and gas produced from oil wells with subsequent determination of the well's flow rate. The installation allows you to control the operation of wells based on the availability of liquid and gas supply and ensures the transmission of this information, as well as information about the accident, to the control center.

3. What inscriptions are on the doors of the AGZU premises?

Outside the process room, warning signs must be painted in red paint, the inscriptions “Explossion class B-1a and fire hazard category” and “Flammable”, grounding signs, ventilate for at least 20 minutes before entering, energy safety, responsible for fire safety

4. What is SPPK, explain it, what is it for, what pressure is it calibrated for? (for some reason no one asked about calibration dates!)

SPPK – separation (special?) spring safety valve. The valve is calibrated (if the pressure in the vessel is from 30 - 60 atm., 10% - 15% more than the permitted pressure. If the pressure in the vessel is up to 30 atm., then 10% more than the permitted pressure. The factory value is written on the SPPK plate number, set pressure and date of actual calibration. Calibration period is once every 2 years. The valve is installed to prevent overpressure.

Specially spring safety valve installed on vessels, apparatus and pipelines of workshops / areas /

Design spring valve must provide a device for checking the proper operation of the valve in working condition by forcibly opening it during operation of the vessel.

The need and timing for checking the operation of the valve in working condition by forced opening should be determined by: at least once every 10 days, for vessels (devices) technological installations(DNS, KNS, UPSV, UPN, etc.), and at least once every 3 (three) days for separation tanks AGZU. The time and date of checking the operation of the valve in working condition, by forced opening, must be recorded by the maintenance personnel with an entry in the logbook (well pad maintenance logbook).

Adjustment safety valves on pressure the beginning of opening - set pressure/cotton/ is produced at a special stand.

Set pressure valve is determined based on the operating pressure in the vessel, apparatus or pipeline, on the basis of the approved technological regulations.

Council of Chief Mechanics of Enterprises
oil refining
and petrochemical industry

INSTRUCTIONS. IPKM-2005

“Procedure for operation, inspection and repair
spring safety valves,
membrane safety
oil refinery devices
and petrochemical enterprises
Ministry of Industry and Energy of Russia"

Moscow 2006

COUNCIL OF CHIEF MECHANICS OF ENTERPRISES
OIL REFINING AND PETROCHEMICAL
INDUSTRY

PUBLIC CORPORATION
"ALL-RUSSIAN RESEARCH
AND DESIGN AND TECHNOLOGICAL INSTITUTE
EQUIPMENT FOR OIL REFINING AND
PETROCHEMICAL INDUSTRY"
(JSC "VNIKTIneftekhimoborudovanie")

Instructions. IPKM-2005

“Procedure for operation, inspection and repair of spring
safety valves, diaphragm safety valves
devices of oil refining and petrochemical enterprises
Ministry of Industry and Energy of Russia"

Volgograd - 2006

On review of regulatory and technical documentation

Directorate for Supervision of Oil and Gas Production, Refining and Trunk Facilities pipeline transport reviewed the instructions ((Procedure for operation, inspection and repair of spring safety valves, membrane safety devices oil refining and petrochemical enterprises of the Ministry of Industry and Energy of Russia" (IPKM-2005), approved by the Chairman of the Council of Chief Mechanics of Oil Refining and Petrochemical Enterprises on January 23, 2006, minutes of a technical meeting to review the said instruction dated September 30, 2005 with the participation of specialists from oil refining and petrochemical enterprises and specialists of OJSC "VNIKTIneftekhimoborudovanie", comments of OJSC "NIIKHIMMASH" to the instructions (letter dated 04/26/2006 No. 7064-31-5-31) and changes and clarifications made to the instructions of OJSC "VNIKTIneftekhimoborudovanie" (letter dated 06/19/2006 No. 13/731) and reports the following.

In accordance with Article 17 of the Federal Law of December 27, 2002 No. 184-FZ “On Technical Regulation”, standards of organizations, including public ones, are developed independently, in accordance with the requirements of national norms and rules and are not subject to coordination with Rostechnadzor.

The submitted document does not contradict the requirements of national norms and regulations. It has industrial safety and can be used as a recommendation document for organizations operating hazardous production facilities in the oil refining and petrochemical industries instead guidance document RUPC-78

Preface

1. DEVELOPED by the Open Joint-Stock Company "VNIKTIneftekhimoborudovanie" taking into account proposals from oil refining and petrochemical enterprises of the Ministry of Industry and Energy of Russia.

DEVELOPERS:

A.E. Foliyants; N.V. Martynov; Yu.I. Shleenkov; N.N. Tolkachev; A.E. Starodubtsev; G.V. Gorlanova; S.V. Evgrafova; N.S. Goleva - OJSC "VNIKTIneftekhimoborudovanie";

A.A. Shatalov - federal Service on environmental, technological and nuclear supervision;

B.S. Kabanov, V.L. Sokolov - LLC PA "Kirishinefteorgsintez",

S.O. Malikov - Lennihimmash LLC.

2. Put into effect by order of the enterprise.

3. With the entry into force of the “Instructions”, the effect of RUK-78 “Guidelines for the operation, inspection and repair of spring safety valves” is canceled.

4. These instructions are mandatory for all enterprises in the oil refining and petrochemical industries.

1 area of ​​use

1.1 This instruction provides for the procedure for operation, supervision, inspection and repair of spring safety valves (SPV), membrane safety devices (MPD) installed or installed on vessels, apparatus, pipelines, pumps, compressors and other types of equipment of oil refining and petrochemical enterprises of the Ministry of Industry and Energy of Russia.

1.2 The instructions do not apply to safety valves of steam boilers, steam superheaters and economizers with an operating pressure of more than 0.07 MPa (0.7 kgf/cm 2) and hot water boilers with water temperatures above 115 °C, which are subject to the “Rules for Construction and safe operation steam and hot water boilers", as well as safety valves of steam and hot water pipelines with a working steam pressure of more than 0.07 MPa (0.7 kgf/cm 2) or hot water with water temperatures above 115 °C, which are subject to PB 10-573-03.

2 Normative references

3.1.7 Diaphragm safety device(MPU) - a device consisting of a bursting safety membrane (one or more) and its fastening unit (clamping elements) assembled with other elements, providing the necessary weight relief working environment at a certain response pressure.

3.1.8 MPU vacuum- a special membrane safety device used in cryogenic tanks and pipelines to protect the thermal insulation cavity from increased pressure in an emergency.

3.1.9 Safety membrane (MP)- MPU safety element, which collapses at a given pressure and frees up the necessary flow area for communication of the protected vessel (pipeline) with the discharge system.

3.1.10 Bursting membrane (MR)- flat or dome-shaped MP, working to break under the pressure acting on its surface.

3.1.11 Flapping membrane (MX)- dome-shaped MP. working to lose stability (clap) under pressure acting on a convex surface. Losing stability, the membrane is cut using knife blades or torn along a previously weakened section.

3.1.12 Clamping elements- parts used to secure (clamp) the MP along the edge annular section.

3.1.13 Conditional pass Du (DN)- nominal internal diameter of the pipeline connected to the fittings;

3.1.14 Conditional pressure Ru (PN)- greatest overpressure at an ambient temperature of 293K (20 °C), at which long-term operation of vessels, fittings and pipeline parts having specified dimensions, justified by strength calculations for the selected materials and their strength characteristics corresponding to a temperature of 293K (20 °C) is permissible;

3.1.15 Internal (external) pressure- pressure acting on the inner (outer) surface of the vessel wall.

3.1.16 Design pressure of the vessel (apparatus), pipelineR race- excess internal or external pressure for which the strength is calculated *

3.1.17 Permitted pressure of the vessel (apparatus), pipeline P times- maximum excess permissible internal or external pressure, established based on the results of technical examination or technical diagnostics.*

3.1.18 Operating pressure of the vessel (apparatus), pipeline R slave- excessive maximum internal or external pressure that occurs during the normal course of the technological process (pressure, temperature of the working medium, etc.) without taking into account the hydrostatic pressure of the working medium and without taking into account the permissible short-term excess pressure during the operation of the safety valve or other safety devices*.

*Note. Operating, permitted and design pressures are assigned from the condition R slave ≤ P times ≤ R race.

3.1.19 Design temperature of the wall of the vessel (apparatus), pipeline T races- the highest wall temperature at which permissible stresses are determined and strength calculations are carried out.

3.1.20 Operating temperature of the wall of the vessel (apparatus), pipeline T slave- wall temperature that occurs during the normal course of the technological process.

3.1.21 Permitted temperature of the vessel, pipeline T size- operating temperature at the permitted pressure, established based on the results (pipeline inspection) or technical diagnostics;

3.1.22 Set pressure (opening pressure) of the safety valvePvcm- excess pressure at which the safety valve makes the first pop during adjustment on the bench with compressed air (adjustment spring pressure) or begins to lose its tightness in the valve when testing with water.

3.1.23 Safety valve full opening pressure P 1 - excessive maximum pressure in front of the safety valve when it reaches its full opening.

3.1.24 Pressure behind safety valve R 2 - excess pressure directly at the outlet of the exhaust fitting of the safety valve.

3.1.25 Excessive pressure in the relief system R Sat - maximum pressure in the discharge manifold (flare or candle).

3.1.26 MPU response pressure ( RSrab.) - pressure at which the membrane should collapse (rupture). Indicated together with the response temperature.

3.1.27 Maximum spring deflection- spring compression, at which the gap between the middle coils of the spring does not exceed 0.1 of the diameter of the rod.

3.1.28 Designated membrane service life- calendar duration of operation, upon reaching which the membrane should be replaced, regardless of its technical condition.

4 General provisions

4.1 At each enterprise or production facility, if it is isolated, instructions for the operation, inspection and repair of spring safety valves and MPUs are developed and approved by the chief engineer (technical director).

4.2 Installation of safety valves on vessels, apparatus and pipelines operating under excess pressure is carried out in accordance with current regulations regulatory documents and safety rules. The number, design, installation location of valves, MPU and direction of discharge are determined by the project.

4.3 Safety valves and MPUs are supplied by manufacturers with a passport and instructions (manual) for use. The passport, along with other information, indicates the service life, valve flow coefficient for compressible and incompressible media, as well as the area to which it is assigned. The manufacturer must have permission to use.

4.4 The diameter of the fitting for the safety valve is taken to be no less than the diameter of the valve inlet pipe.

4.5 The diameter of the valve outlet pipe is taken to be no less than the diameter of the valve outlet fitting.

When installing several safety devices on one branch pipe (pipeline), the cross-sectional area of ​​the branch pipe (pipeline) must be at least 1.25 of the total cross-sectional area of ​​the valves installed on it.

In the case of combining the outlet pipes of valves installed on several devices, the diameter of the common manifold is calculated based on the maximum possible simultaneous discharge of the valves, determined by the project.

4.6 The riser diverting the discharge from the safety valve into the atmosphere is protected from precipitation and at the lowest point a drainage hole with a diameter of 20 - 50 mm is made to drain the liquid.

The direction of discharge and the height of the outlet riser are determined by the design and safety rules.

4.7 Sampling of the working medium from branch pipes and sections of connecting pipelines from the vessel to the valve on which safety valves are installed is not allowed.

4.8 The fittings in front of (behind) the safety device can be installed provided that two safety devices are installed and locked to prevent their simultaneous shutdown. In this case, each of them must have a throughput in accordance with the requirements of the “Rules for the Design and Safe Operation of Pressure Vessels”.

When installing a group of safety devices and fittings in front of (behind) them, the blocking must be performed in such a way that in case of any valve shutdown option provided for by the design, the remaining switched on safety devices have a total capacity in accordance with the requirements of the “Rules for the Construction and Safe Operation of Pressure Vessels” "

4.9 Heating, cooling, separation and neutralization devices can be installed after the valve. The total reset resistance should not exceed that specified in paragraph.

List of set pressures, frequency of checks and revisions in the form given in the appendix;

Schedule of inspection and repair in the form given in the appendix;

Operational passports in the form given in the appendix;

Passports for MPUs, membranes and springs from manufacturers (stored together with operational passports for valves);

Calculations of the capacity of safety valves (see Appendix) are included in the corresponding passports of vessels (devices), pipelines, pumps, compressors on which the valves are installed.

The following technical documentation is additionally prepared at the LPU:

MPU operation log;

Acts of monitoring the integrity of the safety membrane (free form).

Operating data should be regularly recorded in the membrane operation log:

5.8 In case of absence or loss of the manufacturer’s passport for a valve or spring, it is allowed to draw up new passports (according to the manufacturer’s form) signed by the chief engineer, chief mechanic of the enterprise, senior mechanic of the workshop, foreman of the specialized workshop, section, workshop that carried out the hydraulic test, technical supervision representative. To draw up a passport, the valve must be disassembled, inspected, a hydraulic test and a spring test have been carried out on the valve, and, if necessary, it must be adjusted. Data on the technical characteristics of the safety valve and spring are filled in based on their factory markings, compliance of the geometric dimensions with the drawings, manufacturer's specifications for the springs and test results.

In case of absence or loss of the manufacturer’s passport for the MPU or batch safety membranes(MP), it is allowed to draw up new passports (according to the manufacturer’s form) signed by the chief mechanic of the enterprise, the senior mechanic of the workshop, a representative of technical supervision and the chief engineer of the enterprise. To draw up a passport, the MPU must be disassembled and inspected for the absence of visible damage. The data in the passport for the MPU is entered on the basis of the existing markings of safety membranes and fastening devices, for which the MPU is disassembled, inspected for the absence of visible damage, and representatives from the batch of membranes are tested for response pressure. The passport form for LPA is given in the appendix.

5.9 A plate with the following information is securely attached to the body of each valve:

Place of installation (production, workshop number, designation of the apparatus, pipeline according to the technological diagram);

Set pressure Pvcm,

Working pressure in a vessel, apparatus, pipeline R slave.

Membranes for marking are equipped with marking shanks attached to them. The markings on the shanks are applied from the dome side of the membrane using electrographic, impact or other methods that prevent it from being erased during operation. The marking contains the following information:

Name (designation) or trademark of the manufacturer;

Membrane batch number;

Membrane type (MP or MX);

Membrane material;

Nominal diameter Dy (DN) - according to MPU;

Working diameter (Dpab.) - according to that specified in the MPU passport;

Design diameter (Dpacch.) - according to the technical specifications (order) for the MPU;

Minimum and maximum response pressure of membranes in a batch at a given temperature and at a temperature of 20 °C (for all membranes in a given batch).

5.10 Only workers who have passed a knowledge test and are certified in accordance with the current rules are allowed to service safety valves and MPUs. technical devices, where the PC and MPU are installed.

6 Inspection, repair, adjustment and testing of safety valves and MPU. Inspection of clamping tracks

6.1 An inspection of safety valves consists of disassembling, cleaning, troubleshooting parts, testing the inlet part (inlet pipe and nozzle), testing the spring, assembling, adjusting the set pressure, checking the tightness of the valve, testing the valve connections for tightness. The procedure for disassembly and assembly, a list of possible malfunctions in the operation of safety valves and methods for eliminating them are given in the appendix.

Inspection, repair, adjustment, and testing of safety valves are carried out in a specialized repair shop, workshop (site) on special stands in accordance with the instructions for use, inspection and repair of spring safety valves. An approximate list of equipment and mechanisms of a specialized workshop, workshop (site) for inspection and repair of safety valves is given in the Appendix.

6.2 The value of the set pressure, the frequency of inspection, repair and adjustment, the installation location, the direction of discharge from the safety valves are indicated in the list of set pressures (see Appendix). The statement is compiled for each production facility of the enterprise, agreed with the technical supervision service, the chief mechanic and approved by the chief engineer (technical director) of the enterprise and stored at the production facility, in a specialized repair shop, workshop (site), in the technical supervision service.

6.3 For valves that have undergone inspection, repair, adjustment and testing, an inspection report is drawn up (see Appendix) with mandatory verification of the actual set pressure with the list of set pressures.

6.4 Valves that have undergone inspection, repair, adjustment and testing are sealed with a special seal kept by the repairman. The locking screws of the adjusting bushings, the detachable connections between the body and the cover and the cover and the cap are subject to mandatory sealing. The seals indicate the month and year of the inspection and the mark of the specialized workshop, workshop (site). The results of the inspection and repair are recorded in the valve’s operational passport.

6.5 Inspection of the MPU includes disassembly, cleaning and degreasing of parts, and troubleshooting of parts. Parts mating to the membrane that have corrosion or cracking must be replaced.

6.6 Frequency of inspection, repair, adjustment and testing of safety valves

6.6.1 The frequency of inspection, repair and adjustment of safety valves is determined taking into account the conditions and experience of their operation, the harmful effects of the working environment (corrosion, freezing, sticking, polymerization), but it should not exceed the time limits established in - except in cases of using MPU to protect safety valves from corrosion.

The designated service life of the safety membrane is determined by the manufacturer of the MPU, taking into account the specific operating conditions of the safety membrane (corrosion rate of the material, the composition of the working environment of the device being protected, the temperature of the environment at the installation site of the safety membrane, the degree of load (the relationship between the operating pressure and the response pressure of the membrane) and the expected load speed (the rate of increase in the pressure of the “explosion” of the medium in the apparatus) upon activation, the nature of the loading of the membrane during operation (static, alternating, pulsating), the rate of creep of the material under specific operating conditions), and is confirmed by calculation.

6.6.2 The rate of corrosion of valve parts is determined based on safety valve inspection data or testing of samples made of similar steel under operating conditions.

6.6.3 Tests of valve detachable connections for tightness are carried out during each revision.

6.6.4 Timing for inspection, repair, and adjustment of safety valves production facility are indicated in the annually compiled schedule in the form given in Appendix B. The schedule is agreed upon with the technical supervision service, the chief mechanic and approved by the chief engineer (technical director).

6.6.5 Valves received from the manufacturer or from reserve storage must be adjusted on a bench to the set pressure immediately before installation on vessels and pipelines. After the expiration of the preservation period specified in the passport, the valve must be subjected to inspection with complete disassembly.

6.7 Defects of safety valve and MPU parts

6.7.1 Valve parts must not have burrs, nicks, dents, or bends. In case of damage to the nozzle and spool (nicks, marks, corrosion), it is necessary to restore their surfaces by mechanical processing and subsequent grinding.

6.7.2 The thread of the adjusting screw must be clean and free of nicks. All fasteners with defective threads are replaced.

6.7.3 Safety valve springs are checked visually for cracks and corrosion pits.

Springs are considered unsuitable for use if dents, nicks, cracks, and transverse risks are found during inspection.

The perpendicularity of the ends of the spring axis must be within the tolerance specified in the appendix, in the tables and.

6.7.4 During each inspection of the safety valve, the springs are subjected to control, including:

Threefold compression by a static load causing maximum deflection, while the spring should not have a residual deformation (shrinkage) of more than 1.5% of the original height of the spring in a free state;

Compression of the maximum working static load specified in the passport or specification for the springs, the axial movement must be within the limits specified in the appendix, in the tables and;

Checking for the absence of surface cracks using magnetic particle or capillary flaw detection; the need for inspection is determined by the instructions of the enterprise operating the safety valve.

In addition to magnetic particle or penetrant flaw detection, springs can be checked for surface cracks by immersing the spring for 30 minutes. in kerosene and then wipe it dry, after which the spring is sprinkled with chalk powder. Dark streaks on the surface of the chalk indicate the presence of surface cracks; such a spring is rejected.

Magnetic particle and capillary flaw detection are carried out in accordance with RDI 38.18.017-94 and RDI 38.18.019-95.

6.7.5 If traces of corrosion or wear are visually detected on the valve body, it is subjected to thickness testing. Rejection of the housing based on wall thickness, as well as the sealing surfaces of the flanges, is carried out in accordance with clause 13.52 of RD 38.13.004-86.

6.7.6 When inspecting the MPU or replacing the membrane and detecting corrosion damage or cracking of the surfaces of the clamping rings mating with the membrane, the clamping rings must be replaced.

Fasteners (studs, nuts) are rejected if they are worn out, threads are chipped, or turnkey surfaces are worn out.

6.8 Adjusting safety valves

6.8.1 Adjustment of safety valves to the set pressure is carried out on a special stand. The installation pressure is determined by the project in accordance with the “Rules for the Design and Safe Operation of Pressure Vessels”.

Rice. 3. Installation diagram of the MPU with a three-way valve in front of the valves.

7.4 MPU should be installed on branch pipes or pipelines directly connected to the vessel.

7.5. The connecting pipelines of the MPU should be protected from freezing of the working medium in them.

7.6. MPU should be placed in places that are open and accessible for inspection, maintenance, installation and dismantling.

List of organizations specialized in the design and manufacture of membrane safety devices.

A safety valve (hereinafter referred to as PC) is a pipeline fitting primarily direct action(there are also PCs controlled by pilot or pulse valves), designed for emergency bypass (dumping) of the medium when the pressure in the pipeline exceeds a predetermined one. After releasing excess pressure, the PC must close hermetically, thereby stopping further release of the medium.

In these instructions, 2 terms are used:

1. Setting pressure (hereinafter referred to as Рн) – this is the greatest redundant pressure at the valve inlet (under the spool) at which the valve is closed and sealed. When pH is exceeded, the valve must open to such an amount as to ensure the required flow of medium to reduce the pressure in the pipeline or vessel.

2. Opening start pressure (hereinafter referred to as Рн.о.) is the pressure at which the so-called “pop” in industrial jargon occurs, i.e. the pressure at which the valve spool opens by a certain amount, releases some of the pressure and then closes back. “Cotton” is clearly distinguishable in gaseous media; in liquid media, this concept is defined with great difficulty.

Checking the settings and functionality must be carried out at least once every 6 months in accordance with GOST 12.2.085 “Pressure vessels. Valves are safety safety requirements."

Pressure pH can only be checked on so-called "full consumable» stands, i.e. those that repeat the operating parameters of the pipe (vessel) in terms of pressure and flow. Considering the variety of objects on which PCs are installed, even within one enterprise, it is not possible to have such a number of stands.

Therefore, when checking and configuring the PC, the determination of pressure pH is used. O. Based on numerous experiments over many years of practice, it has been established that Rn. O. should be higher than pH by no more than 5-7% (10% in Western standards).

Checking valves for functionality and pressure pH. O. held at "non-expendable" stands, typical representative which is a stand for testing and adjusting safety valves SI-TPA-200-64 produced by the Design Bureau pipeline fittings and special works."

Stand for testing and adjusting safety valves SI-TPA-200-64 ensures the following pneumatic tests (medium - air, nitrogen, carbon dioxide, other non-flammable gases):

- tests for tightness of the seat-body connection;

- tests for tightness of the seat-spool pair (tightness in the valve);

- performance tests (operation tests);

- settings for response pressure.

It is possible to manufacture a stand complete with water testing.

The stand provides testing of pipeline fittings with a flange type of connection (threaded connection as an option)

maximum diameter 200. The maximum test pressure depends on the type of pressure regulator supplied as part of the control panel, basic equipment control panel – regulator 0 to 1.6 MPa. Testing of valves with union connection is carried out using an adapter (not included in the delivery set).

The test pressure source is not included in the scope of delivery.

It is possible to equip it with a pressure source according to the customer’s technical specifications.

Test stand SI-TPA-200-64 passed UkrSEPRO certification, supplied complete with operating instructions and passport.

Adjustment (setting) of safety valves to operate at a given pressure is carried out:

Before installation. After a major overhaul, if safety valves or their major renovation(complete disassembly, grooving of sealing surfaces, replacement of chassis parts, etc.), in case of replacing a spring. During periodic inspection. After emergency situations caused by PC failure.

The actuation of the valves during adjustment is determined by a sharp pop accompanied by the noise of the ejected medium, observed when the spool is torn away from the seat. For all types of PCs, operation is controlled by the beginning of the pressure drop on the pressure gauge.

Before starting work on setting up (checking) the PC, it is necessary to instruct the shift and adjustment personnel involved in the work on adjusting the valves.

Staff should be well aware design features PCs subject to adjustment and the requirements of their operating instructions.

GENERAL PROCEDURE FOR CHECKING SAFETY VALVES.

Install on the stand a flange of the type that matches the type of flange of the PC being tested. Install the required gasket. Install the valve onto the stand flange. Tighten the stand screw until the PC is fully secured in the clamps. Create the maximum possible backpressure force on the PC spool. Block the access of the medium under the valve spool using a shut-off device. Supply the medium to the control panel and set the required response pressure (start of opening) at the outlet of the control panel. Open the shut-off device and supply the test medium under the PC spool. Reduce the back pressure force until the valve actuates. Block access to the medium under the PC spool. Re-supply the medium under the PC spool - the valve should operate at the required pressure. Repeat steps 10 and 11 at least 3 times. If it is not possible to adjust the PC properly, return the valve to the RMC for additional grinding of the seat and (or) spool. If the functionality of the PC is confirmed, remove the PC from the stand, having previously shut off the supply of medium under the spool and to the control panel. Fill out the PC operational documentation and the bench work log. Seal the PC and backpressure adjustment mechanisms. Turn off the stand. Drain the water (condensate) from the cavities of the stand, wipe dry, and apply protective lubricant. Ensure that the stand is protected from dust and moisture until the next use.

FEATURES OF ADJUSTING LEVER-WEIGHT VALVES.

Direct-acting lever-load valves are adjusted in the following sequence:

1. The weights on the valve levers are moved to their extreme position.

3. The weight on one of the valves is slowly moved towards the body until the valve is activated.

4. After closing the valve, the position of the weight is fixed with a locking screw.

5. The pressure rises again and the pressure value at which the valve operates is checked. If it differs from the required one, the position of the weight on the lever is adjusted and the correct operation of the valve is re-checked.

6. After completing the adjustment, the position of the weight on the lever is finally fixed with a locking screw. To prevent uncontrolled movement of the load, the screw is sealed.

7. If the backpressure created by the load is insufficient, an additional weight is installed on the lever of the adjustable PC and the adjustment is repeated in the same sequence.

FEATURES OF ADJUSTING DIRECT-ACTING SAFETY VALVES.

1. The protective cap is removed and the adjusting screw is tightened as much as possible (“to the bottom”).

2. The pressure on the bench pressure gauge is set to 10% higher than the calculated (permitted) pressure.

3. By turning the adjusting sleeve counterclockwise, the compression of the spring is reduced to a position at which the valve will operate.

4. The pressure rises again and the value at which the valve operates is checked. If it differs from the required one, then the spring compression is adjusted and the valve is re-checked for operation. At the same time, the pressure at which the valve closes is monitored. The difference between the actuation pressure and the closing pressure should be no more than 0.3 MPa (3.0 kgf/cm2). If this value is greater or less, then the position of the adjusting sleeve must be adjusted.

For this:

For TKZ valves, unscrew the locking screw located above the cover and turn the damper bushing counterclockwise to reduce the drop or clockwise to increase the drop;

For PPK and SPPK valves, the pressure difference between the actuation and closing pressures can be adjusted by changing the position of the upper adjusting sleeve, which is accessed through a hole closed with a plug on the side surface of the body.

5. After completing the adjustment, the position of the adjusting screw is locked using a locknut. To prevent unauthorized changes in the spring tension, a protective cap is installed on the valve, covering the adjusting sleeve and the end of the lever. The bolts securing the protective cap are sealed.

FEATURES OF ADJUSTMENT OF PULSE-SAFETY DEVICES WITH PULSE VALVES USED IN POWER PLANTS.

Ticket No. 8

Requirements for the safe performance of work when conducting hydraulic testing of the hydraulic control system in the VNK.

1. Hydraulic testing is aimed at checking the strength of the vessel elements and the tightness of the joints. Vessels must be submitted for hydraulic testing with fittings installed on them.

4.2. Hydraulic testing of vessels is carried out only if the results of external and internal examinations are satisfactory.

4.3. Fill the vessel with water. When filling a vessel with water, the air must be completely removed. For hydraulic testing of vessels, water with a temperature not lower than +5ºС and not higher than + 40ºС should be used, if technical conditions no specific temperature value allowed under the condition of preventing brittle fracture is indicated. The temperature difference between the vessel wall and the surrounding air during testing should not cause moisture condensation on the surface of the vessel walls. By agreement with the vessel design developer, another liquid can be used instead of water.

4.5. The pressure in the vessel should be increased gradually. The rate of pressure rise must be specified in the installation and operating instructions.

Usage compressed air or other gas to raise pressure is not allowed.

The test pressure must be monitored by two pressure gauges, one of which must be installed on the top cover (bottom) of the vessel. Both pressure gauges must be of the same type, measurement limit, same accuracy classes, and division values.

4.6. Maintain the vessel under test pressure for 5 minutes, unless otherwise specified by the manufacturer.

4.7. Reduce the pressure to the design (permitted) value and inspect the outer surface of the vessel, all its detachable and welded connections.

Tapping the walls of the body, welded and detachable joints of the vessel during testing is not allowed.

4.8. The vessel is considered to have passed the hydraulic test if the following is not detected:

Leaks, cracks, sweating tears in welded joints and in the base metal;

Leaks in detachable connections;

Visible residual deformations, pressure drop on the pressure gauge.

4.9. The vessel and its elements, in which defects were identified during testing, are subjected to repeated hydraulic tests with test pressure after their elimination.

In cases where a hydraulic test is not possible, it is permitted to replace it with a pneumatic test (air or inert gas). This type of test is allowed subject to its control by the acoustic emission method (or another method approved by the State Mining and Technical Supervision Authority of Russia).

During pneumatic testing, precautions are taken: the valve on the filling pipeline from the pressure source and pressure gauges are taken outside the room in which the vessel being tested is located, and people are removed to a safe place during the test pressure test of the vessel.

Frequency of SPPK calibration.

Along with the technical examination of the vessels, safety valves must be calibrated (at least once every 2 years). The number of safety valves, their dimensions and capacity must be selected according to calculations so that pressure does not build up in the vessel exceeding the excess pressure by more than 0.05 MPa (0.5 kgf/cm2) for vessels with pressure up to 0. 3 MPa (3 kgf/cm2), by 15% - for vessels with pressure from 0.3 to 6.0 MPa (from 3 to 60 kgf/cm2) and by 10% - for vessels with pressure over 6.0 MPa (60 kgf/cm2). The calibration pressure of safety valves is determined based on the permitted pressure in the vessel.

At what pressure is the SPPK calibrated?.

The number of safety valves, their sizes and capacity must be selected according to calculations so that vessel pressure was not created exceeding the design one by more than 0.05 MPa (0.5 kgf/cm2) for vessels with pressure up to 0.3 MPa (3 kgf/cm2), by 15% for vessels with pressure from 0.3 to 6.0 MPa (from 3 to 60 kgf/cm2) and by 10% - for vessels with pressure above 6.0 MPa (60 kgf/cm2).

When safety valves are operating, the pressure in the vessel may be exceeded by no more than 25% of the working pressure, provided that this excess is provided for by the design and is reflected in the vessel passport.

The procedure for preparing a vessel for inspection.

The person responsible for good condition and safe operation must ensure the preparation of the vessel for technical inspection and participate in it.

2.1. Work inside the vessel must be carried out in accordance with the work permit.

2.2. Before internal inspection and hydraulic testing, carry out the following

current works:

Stop the vessel;

Cool (warm);

Free from the environment that fills it;

Disconnect plugs from all pipelines connecting the vessel to a pressure source or other vessels;

Steam with live steam until the hydrocarbon content is below 300 mg/m 3 and the oxygen content is less than 20% by volume;

Clean the vessel down to metal.

Vessels working with harmful substances 1st and 2nd hazard classes according to GOST 12.1.007, before starting any work inside, as well as before internal inspection, they must undergo mandatory processing (neutralization, degassing) in accordance with instructions for the safe performance of work, approved by the chief engineer .

Lining, insulation and other forms of corrosion protection must be partially or completely removed if there are signs indicating the possibility of material defects. power elements vessel structures (lining leaks, lining holes, traces of insulation being wet, etc.). Electrical heating and the vessel drive must be turned off;

Remove devices that impede external and internal inspection of vessels (coils, stirrers, jackets, plates, etc.).

The possibility of removing welded devices and their subsequent installation in place must be indicated in the technical documentation and in the “Installation and Safe Operation Instructions” of the plant.

manufacturer;

Vessels with a height of more than 2 m must be equipped with necessary equipment, providing safe access to all parts of the vessel.

4.In what cases is it permissible to install shut-off valves between the SRD and PPK.

The fittings in front of (behind) the safety device can be installed provided that two safety devices are installed and locked to prevent them from being turned off simultaneously. In this case, each of them must have the capacity provided clause 5.5.9 Rules

When installing a group of safety devices and fittings in front of (behind) them, the blocking must be performed in such a way that, in case of any valve shutdown option provided for by the design, the remaining switched on safety devices have the total capacity provided for in clause 5.5.9 of the Rules.

5.What data is applied by the manufacturer to the DDS? ,

What data is applied by the manufacturer to the DDS.

The manufacturer puts the following data on the DDS:

Manufacturer's name;

Name of the vessel;

Design, test and working pressure;

Working temperature;

Mass and volume;

Date of manufacture.

Figure 3.1. - Manufacturer's data

Answer:
Hello. Calibration is carried out on the basis of the factory

Operating manuals (instructions).

PB 03-583-03 for membrane devices also applies.

There are no similar PBs in the oil and gas industry. It is possible to use the “Operating Procedures...” you specified, if it applies to the oil and gas industry.