Мониторинг и ликвидация межколонных давлений

Полный текст

Introduction

The quality improvement of well cementing and casing leak tightness with the development of new technologies and with the increase of well depth gets more urgent.

Intercasing pressure (hereinafter referred to as ICP) take place at most of the fields, which is especially typical for gas and gas-condensate fields. Both technogenic factors (quality of well construction, materials and equipment used) and natural factors, independent of human activity, influence the occurrence of ICP [1].

The authors of the work [2] assume that the main causes of the appearance of intercasing pressures are:

- leaky casing threaded joints;

- leakiness of wellhead gaskets of casing strings;

- gas migration during the waits on cements (here in after WOC).

During the WOC, a contraction occurs, which can lead to serious violations of the integrity of the cementing slurry. This phenomenon appears mainly in the WOC in the conditions of fluid-resistant layers, which contain dense and low-permeable rocks. The results of this phenomenon may be shrinkage deformations [3].

It is necessary to pay special attention to the ways of formation fluid migration to the surface regardless of the cause of ICP, the main of which are:

- cement ring channels formed during cement stone formation due to low sedimentation stability of cementing slurry;

- micro-gaps in the contact between the cement and the casing, due to insufficient adhesive capacity of the cement, as well as those formed during operations inside the cemented casing, such as drilling out the cement plug and further deepening of the well. The formation of micro gaps is also promoted by casing pressure tests to check for leaks, determination of well injectivity, and stimulation activities;

- casing leakage in the body or threaded joints;

- leakage of casing head in places where sealing elements are installed and fluid flow from annular space to intercasing annulus (hereinafter referred to as ICA) or from one ICA to another;

- impact of temperature factor during startup and shutdown of wells.

There is also a necessity to be taken into account that casing is pressurized with liquid, and in this case, the casing and intercasing annulus are hermetically sealed.

According to theory, there should be no ICP in such situation, but since gas permeability is much higher than liquid permeability, so gas penetrates where liquid does not filter.

Furthermore, there are a number of important but poorly understood factors which undoubtedly affect the occurrence and magnitude of ICDs, which include: electric fields that change over time due to changes in:

- metal intensity of the deposit, changes in the subsurface and in the environment;

- physical and chemical processes taking place in ICA;

- osmotic phenomena in the cement stone.

The reasons mentioned above confirm that cementing quality of wells will directly influence the occurrence of ICP. As the problem of improving the quality of well cementing was discussed in papers [4–7], and at present there are many wells in Kazakhstan, which have problems with cementing in gas and gas-condensate wells, the purpose of this work is to study and eliminate wells with ICP.

The problem of intercasing pressures occurs in many wells of our republic. For example, at the North Buzachi oil field, which is located in Mangistau region, out of 97 wells drilled since the discovery and up to 2000 years, 72 wells were abandoned due to poor quality of well cementing. At 15 wells drilled from 2003 to 2004 there were problems with the formation of griffins and the presence of intercasing pressures [1].

At the Amangeldy field, operation of wells with intercasing pressure is carried out in accordance with the "Program of well management with intercasing pressure at the Amangeldy field", developed by NIPIneftegaz JSC in 2008.

In order to minimize risks when operating wells with ICP and to ensure the safety of personnel servicing the wells, as well as the negative impact on the environment, AmangeldyGas LLP conducted monitoring of wells with ICP, provided for by the Program [8, 9].

Under the calculation of maximum permissible pressures (MPP), conducted in accordance with the "Methodology for determining the categories of emergency wells with intercasing pressure at the Amangeldy field" and the category of danger of wells with ICD was determined.

The maximum average pressure recorded between the production and intermediate casing for the period from 2003 to 2012 was 6.8 MPa (well 117), and between the intermediate casing and surface casing – 2.7 MPa (well 103). The maximum MAP percentage was 31% (well 117) in 2006. At all other wells the percentage of MAP was much lower, so practically all wells were classified as category 4 ICP, since the recorded MCPs were less than 25% of the MAP.

In 3 wells (106, 111, 16-G), ICPs were practically absent during the analyzed period. In 7 wells (105, 111, 117, 120, 121, 2-G, 6-G) pressure was observed mainly only between the production and intermediate strings. Pressures in both spaces during the whole period of analysis were registered in 7 wells (101, 103, 108, 112, 113, 114, 122).

Therefore, as of 01.05.2012 all wells of the field belonged to the 4th category of danger ICP. Therefore, with the purpose of control over well operation, creation of safe working conditions for personnel and environmental protection when working at wells with ICP, and considering that 21 wells of the 4th category were identified in the field the following recommendations were developed [10]:

- it is recommended to carry out weekly monitoring of pressures in intercasing annulus;

- wells that do not have ICPs should be monitored on a weekly basis;

- in case of new wells with high pressure in the interwell space or growth of interwell pressures of more than 25% of MPP, to transfer to another category, assess the technical condition of the well, carry out work to reduce or eliminate high pressure in the interwell space and continue observation with weekly monitoring.

In 2016, Yu. A. Daribayev and employees of "Clinal" LLP conducted monitoring of wells in the field, or rather work on the research and diagnosis of the causes of intercasing pressure in several wells of Amangeldy field.

On well No.121 of Amangeldy field were conducted work on research and diagnosis of the causes of the occurrence of intercasing pressure.

The work is carried out by the autonomous laboratory IDL-1[8, 11].

1 stage of research – complete study of geological and tectonic characteristics of the well, data of materials during well drilling, logging, conclusion of GIS, LLS, CBL, materials of work performed on the well, gas compositions coming out of the intercasing annulus (hereinafter – ICA).

The second stage of the research is determining the causes of ICP by wellhead injection of the technological solution.

The injectivity of the wellbore was usually determined in two ways:

- by the volume of injected solution providing constant pressure in the ICP;

- by initial pressure recovery.

The first method is to pump such volumes of process fluid that ensure constant pressure in the wellbore packer. In this case, its inflow rate, i.e. injectivity, will be equal to the rate of fluid outflow from the ICP through micro channels to the source of interwell pressure. This method allows pumping at maximum pressure and fluid supply to the ICP. The disadvantage of this method is difficulty to keep constant pressure in ICP because of spontaneous change of injectivity, on which the value of pressure at the wellhead depends.

The second method can be implemented at any pressures in ICP (below the maximum allowable values). It is relatively simple in realization and allows to determine injectivity of the well more accurately. For this purpose, it is necessary to start dosing pump and pump solution up to pressure in MCP equal to the preset one (Pmax). Then the pumping is stopped (t₁) and the pressure drop to a certain value or stabilization (Pmin) is recorded. After that the dosing pump is started and the solution (liquid) is pumped until the initial pressure Pmax is restored. At the same time fix the volume (Q), pumped liquid and time (t₂) from the pump stop till the moment of pressure restoration (t₁–t₂). If we assume, that the volume of pumped liquid was spent for replacement of hollow space in ICP, the injectivity is defined as quotient of division of pumped liquid volume by total time of pressure drop and recovery. Meanwhile, the average injection pressure is defined as half the sum of maximum and minimum pressures, which were obtained during the work (Fig. 1).

 

Figure 1. Example of determination of injectivity and average pumping pressure

t₁ – time from stopping of pump operation; t₂ – time of pressure restoring; Q – volume of pumped liquid at pressure recovery

 

Determination of injectivity (1):

$q_{ing}=\frac{Q}{t_2-t_1}$ (1)

Average value of intake pressure (2):

$Pavg=\frac{P_{\min }+P_{\max }}{2}$ (2)

The intake capacity of the ICP was determined by the volume of the injected solution until the pressure was restored.

We presented calculations of the depth of penetration (immersion) of the solution injected into the ICP of the well, and the growth of back pressure at the source of ICP, taking into account the injection volume and shrinkage of the cement stone.

1. Cement ring area:

$\begin{array}{l}Scs=\mathrm{0,8}\cdot (d_{1in}^2-d_2^2)=\mathrm{0,8}x\\ x(d_{1in}+d_{2in})\cdot (d_{1in}-d_2)\end{array}$ (3)

where d_1in and d₂ are the inner and outer diameters of the technical and production casing, in cm:

d_1in = d₁ - 2β (4)

where d₁ – outer diameter of the intermediate casing, in cm; β – wall thickness of the intermediate casing, in cm.

2. Total area of vertical microchannels formed as a result of cement stone shrinkage (5):

$\Delta Sy=Scs\cdot \eta$ (5)

where η – maximum shrinkage (η = 0,3%).

3. Depth of solution immersion (Lx) taking into account injection volume (Qp) (6):

$Qp=\Delta Sy\cdot Lx$ (6)

from here:

$Lx=\frac{Qp}{\Delta Sy}=\frac{Qp}{Scs\cdot \eta }$ (7)

4. Calculation of the back pressure value at the source (8):

$P=Lx\cdot \Delta y=\frac{Qp}{Scs\cdot \eta }\cdot ({\gamma }_{р}-{\gamma }_{ф})\cdot {10}^{-3}$ (8)

where γ_p and γ_ф – density of solution and filtrate from ICP, in g/cm³.

Calculation for the conditions of well No.121

d_1in = 32.4 – 2*0.95=30.5 cm;

d₂ = 24.4 cm;

η = 0.3%;

Qp = 1l = 1000 cm³;

γ_p = 1.00 g/cm³;

γ_ф = 0.001 g/cm³;

Scs = 0.8*54.9*6.1 = 268 cm²;

ΔSy =268*3·10^-3 ≈ 0,80 cm²;

Lx = 1000 / 0.8 = 1250 cm = 12.5 m;

ΔP = 1250*1 = 1250 g/cm² or 1.25 atm.

Calculation of the maximum allowable pressure of the solution injection in the ICP.

 

Table 1. Data on well No.121 of Amangeldy field

Casing	Outerdiameter, mm	Descentdepth, m
Conductorpipe	426	30
Surfacecasing	324	450.15
Intermediatecasing	244.5	1300
Operational	168,3 Liner 114	0–1707 1707–2273

 

We take the following values of MPP for calculations, taking into account 50% safety margin. Taking into account production casing wear on work and tear, the maximum allowable pressure is equal to:

$P=\frac{Pcollapse\cdot K}{2}$ (9)

$P=\frac{Pin.lin.y.s\cdot K}{2}$ (10)

where K – coefficient of casing string wear is taken into account depending on well operation life (value – 0.8 is assumed), assuming that corrosion rate is 0.1 mm/year and well operation life is insignificant; 2 – coefficient of 50% safety factor.

 

Table 2. Parameters of triangular threaded casing strings, strength grade D

Casing Structure	Diameter, mm	Descent depth, m	Wall thick-ness	Pressure, MPa
				col-lapse pres-sure	Internal limit yield strength
Conductor pipe	426	30	9.5	3.5	15
Surface casing	324	450.15	9.5	10.9	26.9
Intermediate casing	244.5	1300	10	20.9	37.9
Production casing	168.3 114	0–1707 1707–2273	10.59 7.39	55	58.1

 

For the 24 mm diameter surface casing, the yield strength Pys = 26.9 MPa. For the 244.5 mm diameter intermediate casing, the collapse pressure Pcp = 20.9 MPa.

The maximum allowable pressure in intercasing annulus between surface casing and intermediate casing with allowance for casing strength and aging will be equal to:

P = 26.9*0.8/2 = 10.8 MPa (5)

The maximum allowable pressure of pumping of technological solution in ICP in the well No.121 of Amangeldy deposit should not exceed 10.8 MPa.

To determine injectivity, at the first stages of work, we proposed to use service water. Technical water is collected in a container (100-liter barrel). In order to eliminate the intercasing pressure and to fill microcracks in the cement stone behind the column we used a chemical component of a complex composition (sodium liquid glass Na₂SiO₃ + gelling material blast furnace slag and acid), which is widely used in recent years for liquidation of ICD.

Preparation for work on the well

1. Acceptance of the well for work with indication of pressures in tubing, annulus and intercasing annulus.
2. IDL-1 was installed on the windward side at a distance of 30-50 meters from the wellhead.
3. Warning signs were erected at the site of the work.
4. Measured wellhead pressures.
5. The IDL-1 laboratory through the high pressure hose and the distribution coupling has been connected to the branch of the wellhead No.1.
6. The pressure gauges were installed in the tubing and annular outlet of the wellhead.
7. Pressure sensors are connected to control panel IDL-1 by electric cable.
8. The tank for collecting and disposing of the solution, silicone hose, connects to the distribution sleeve.
9. Starting the pump, filling the discharge line with solution.
10. Pressurize discharge line to pressure of pressure reducing valve.

Carrying out the work

1. Start the dosing pump and increase the pressure in the ICP to 30 bar above the initial pressure.
2. Stopping the dosing pump and observing the change of pressures in all the spaces of the well during the calculated time.
3. After the set time, start the dosing pump and additionally increase the pressure in the ICP by 10–50 atm. At the same time constant monitoring of pressures in tubing and annular space, as well as possible leaks in different units of injection line and wellhead equipment.
4. Pressure build-up up to 150 atm according to work program.
5. After every stop of dosing pump to determine the angle of pressure drop and to calculate the value of intake of ICP.
6. At the end of pumping calculation of pumped technological solution volume.

Results and discussions

Brief information about the well No.121.

 

Table 3. Well design and equipments

Equipment title	Parameters
Conductor pipe	426mm х 30m(TOC to wellhead)
Surface casing	324 mm х 450.15 m (TOC to wellhead).
Intermediate casing	244.5 mm х 1300 m(TOC to wellhead)
Production casing	168.3 mm х (0–1707 m) (TOC -324 m to wellhead)
	114 mm х (1707–2273 m)
Artificial Pit	2273 m
Column head	Wellhead 2-35-324х245х168
Christmastree	CPT6 – 65 х 35 Chl
Tubing suspension	Ø73 mm – 2171.6 m
Нр	4 m

 

After the work were obtained ACBL conclusions: on the intermediate casings: 10.9% of the site has partial cement bonding to the column, 56.8% – solid, 31.6% – bad, 0.7% no cement; on production casing: 11.8% of the site has partial adhesion of cement to the column, 38.7% – solid, 48.2% – bad,0.8% – no cement; gas from the intercasing annulus is not flammable.

Carried out work on the well for the study and elimination of ICP

First day. Study of well case materials: well drilling materials, conclusions of LLS and ACBL, gas characteristics, well construction materials, work done on the well. Manometer readings were as follows P_icp1 = 10 atm, P_icp2 = 5 atm. We bleeded the pressures between the technical and production BOP-1, surface casing and the intermediate casing BOP-2 to 0 atm. When bleeding annular space hereinafter AS-1 at the outlet combustible gas, AS-2 (between the surface casing and the intermediate casing) at the outlet incombustible gas. Further on AS-1/2 was pumped an inhibited solution (process water + BrinePac inhibitor) for flushing and filling of microcracks in the cement stone behind the columns, as well as for improvement of setting quality of chemical components. Capacity AS-1 – 10 liters, AS-2 – 11 liters. We monitored the pressure set.

Second day. Reading of pressure gauge at the well P_icp1 = 12 atm, P_icp2 = 17 atm. We bleeded pressure between the technical and production casing of AS-1, surface casing and intermediate casing of AS-2 to 0 atm. We pumped 4 liters of chemical agent into AS-1. We closed AS-1 under pressure of 100 atm. For reacting and setting of chemical components. We pumped into AS-2 a chemical component (liquid glass + bottom ash) in the amount of 6 liters. We closed AS-2 under pressure of 95 atm for reaction and setting of chemical components. We watched the pressure setting.

Third day. Lowered the pressure in the MCC-1/2 to 0 atm. After restoration of pressure the readings of manometers P_icp1 = 0 atm, P_icp2 = 20 atm. Bleeded pressures in AS-2 to 0 atm. We re-injected 6 liters of chemical component into AS-2. We re-injected AS-2 under pressure of 95 atm. For reacting and setting of chemical components.

 

Figure 2. Dependence of AS injectivity on solution injection pressure in the well No.121

 

Other wells of Amangeldy field were investigated in the same way

The gas composition in the annulus and intercasing annulus are identical. This indicates that the gas in the intercasing annulus is identical to the gas from the Permian Serpukhov horizons. Due to the decrease in injectivity and for further work on liquidation of AS, injection of those solutions was stopped.

Conducted work on the well No.103 on the study and elimination of ICP

First day. Study of materials of the well case: materials of well drilling, conclusions of LLS and ACBL, characteristics of gases, materials of well construction, work done on the well. Manometer readings were as follows P_icp1 = 37 atm, P_icp2 = 25 atm. We bleeded pressure between the technical and production casing of AS-1, between the surface casing and the intermediate casing of AS-2 to 0 atm. While bleeding AS-1 output was incombustible gas, AS-2 output was incombustible gas.

We pumped an inhibited solution (process water + BrinePac corrosion inhibitor) into AS-1/2 to flush and fill microcracks in the cement stone behind the columns, as well as to improve the quality of setting of chemical components. Pressure setting of AS-1, 7 liters, AS-2, 22 liters.

Second day. Pressure gauge readings at the well P_icp1 = 40 atm, R_mkd2 = 29 atm. We bleeded pressure between the technical and production casing of AS-1 and between the surface casing and the intermediate casing of AS-2 to 0 atm. Inhibited solution (process water + BrinePaccorrosion inhibitor) was pumped into AS-1/2 for flushing and filling of microcracks in cement behind the columns, as well as for improvement of quality of setting of chemical components. Pressure setting of AS-1, 17 liters, AS-2, 20 liters.

Third day. Pressure gauges P_icp1 = 40 atm, P_icp2 = 29 atm.

We pressurized AS-2 to 0 atm. Into AS-1 we pumped chemical component (liquid glass + domestic slag) in amount of 20 liters. We closed AS-1 under pressure of 95 atm. For reacting and setting of chemical components. In AS-2 we pumped a chemical component (liquid glass + bottom ash) in an amount of 7 liters. We closed AS-2 under pressure of 90 atm. For reactions and setting of chemical components. During 6 days the observation was carried out and the pressure readings of AS was P_icp1 = 0, P_icp2 = 0, which testifies to the efficiency of the measures applied.

Gas composition in annular and intercasing annulus are identical. This indicates that the gas in the intercasing annulus is identical to the gas from the Permian Serpukhov horizons.

Due to a decrease in injectivity and for further work on liquidation of ICP injection of those solutions was stopped.

 

Figure 3. The diagram of dependence of AS injectivity on fluid injection pressure in the well No.103

 

The carried out work on the well No.101 on research and liquidation of ICP

First day. Study of materials of the well case: materials of well drilling, conclusions of LLS and ACBL, characteristics of gases, materials of well construction, work done on the well. Manometers readings were as follows P_icp1 = 22 atm, P_icp2 = 23 atm. We bleeded pressure between the technical and production casing of AS-1, between the surface casing and the intermediate casing of AS-2 to 0 atm. When stripping AS-1 output was non-flammable gas, AS-2 output was non-flammable gas.

We pumped an inhibited solution (process water + BrinePac corrosion inhibitor) into AS-1/2 to flush and fill microcracks in the cement stone behind the columns, as well as to improve the quality of setting of chemical components. Pressure setting of AS-1, 25 liters, AS-2, 50 liters.

Second day. Pressure gauge readings P_icp1 = 27 atm, P_icp2 = 30 atm. We pressurized between the technical and production casing of AS-1 and between the surface casing and the intermediate casing of AS-2 to 0 atm. When stripping AS-1 output was non-flammable gas, AS-2 output was non-flammable gas.

We pumped an inhibited solution (process water + carrosion inhibitor BrinePac) into AS-1/2 to flush and fill microcracks in the cement stone behind the columns, as well as to improve the quality of setting of chemical components. Efficiency of AS-1 was 27 liters, AS-2 – 18 liters.

Third day. We depressurized AS-1 and AS-2 up to 0 atm. We pumped 12 liters of chemical component (liquid glass + bottom ash) into AS-1. We closed AS-1 under pressure of 100 atm. For reacting and setting of chemical components. In AS-2 the chemical component (liquid glass + domain slag) was pumped in an amount of 7 liters. AS-2 was closed at pressure of 90 atm. For reaction andsetting of chemical components. During 7 days the observation was carried out, and pressure readings of AS were as follows. The pressure readings of the AS were P_icp1 = 0, P_icp2 = 0.

Gas composition in annular and intercasing annulus are identical. This indicates that the gas in the intercasing annulus is identical to the gas from the Permian Serpukhov horizons.

 

Figure 4. The graph of dependence of AS injectivity on fluid injection pressure in the well No.101

 

Due to a decrease in injectivity and for further work on liquidation of ICP, injection of those solutions was stopped.

The carried out work on the well No.105 on research and liquidation of ICP

First day. Study of materials of the well case: materials of well drilling, conclusions of LLS and ACBL, characteristics of gases, materials of well construction, work done on the well. Manometers readings were as follows Picp1 = 15 atm, Picp2 = 5 atm. We bleeded pressure between the technical and production casing of AS-1 and between the surface casing and the intermediate casing of AS-2 to 0 atm. When stripping AS-1 output was non-flammable gas, AS-2 output was non-flammable gas.

We pumped an inhibited solution (process water + BrinePac inhibitor) into AS-1/2 to flush and fill microcracks in the cement stone behind the columns, as well as to improve the quality of setting of chemical components. Capacity AS-1, 6 liters per hour, AS-2, 8 liters per hour.

Second day. Pressure gauge readings Picp1 = 22 atm, Picp2 = 5 atm. We pressurized AS-1 to 0 atm. We pumped 12 liters of chemical component (liquid glass + bottom ash) into AS-1. We closed AS-1 under pressure of 100 atm. to react and setting of chemical components.

Third day. Varied the pressure in the AS-1 and AS-2 to 0 atm. In AS-1 we repeatedly pumped 9 liters of chemical component (liquid glass + bottom ash). We closed MCP-1 under pressure of 100 atm. for reacting and setting of chemical components. In AS-2 we pumped chemical component (liquid glass + bottom ash) in an amount of 21 liters. We closed AS-2 under pressure of 90 atm. For reaction and setting of chemical components.

 

Figure 5. Dependence of AS injectivity on fluid injection pressure in the well No.105

 

The gas composition in the annulus and intercasing annulus spaces are identical. This indicates that the gas in the intercasing annulus is identical to the gas from the Permian Serpukhov horizons. In connection with the reduction of injectivity and for further work on liquidation of ICP, injection of those solutions was stopped.

Conclusion

The AS has a microchannel through which gas migrates to the surface. The study revealed that the injectivity of microchannels is 6 liters per hour at a pressure of 70–95 atm. As a result of filling of the channel with chemical component, injectivity of AS and gas migration to the wellhead decreased.

According to the results of the study, the cause of intercasing pressure is migration of gas through the contact zones of cement rock from the formation to the surface through micro channels in AS from Permian and Serpukhov horizons.

Intercasing pressure appeared due to poor-quality cementing of technical and production casing and under-reaming of cementing slurry behind the casing strings.

While performing job on elimination of intercasing pressure at well No.121 of Amangeldy oil field the chemical component (Na₂SiO₃ + gelling material blast-furnace slag-vacuum) was injected, the injectivity of AS gradually reduced from 4 to 2 liters per hour. The chemical component filled in the microcracks of the cement stone, and it caused the stoppage of gas migration in AS-1/2.

The chemical component (Na₂SiO₃ + gelling material – blast furnace slag – vinegar) was injected into well No.105 of Amangeldy deposit while performing work on liquidation of intercasing pressure, the flow rate of BF-1/2 was gradually reduced from 4 to 1/2 liters per hour. The chemical component filled in the microcracks of the cement stone, and this was the reason for stopping the migration of gases in AS-1/2.

At well No.103 of Amangeldy field while performing work on elimination of intercasing pressure, a chemical component (Na₂SiO₃ liquid sodium glass + gelling material blast furnace slag-vinegar) was pumped, the flow rate of AS gradually decreased from 4 to 2 liters/hour. The chemical component filled in the microcracks of the cement stone, and it was the reason of stopping the migration of gases in AS-1/2.

At well No.101 of Amangeldy deposit while performing operations on elimination of intercasing pressure, the chemical component (sodium Na₂SiO₃ + gelling material blast-furnace slag-vacuum) was injected, the rate of flow of AS gradually reduced from 3 to 2 liters/hour. The chemical component filled the microcracks in the cement stone, and this was the reason for stopping the migration of gases in AS-1/2.

For effective setting of the chemical component in the intercasing annulus it is not recommended to carry out any technological operations related to the intercasing annulus (bleeding, flushing, pressure testing, blowing) within 3 months from the date of delivery of the well.

ДОПОЛНИТЕЛЬНО

Источник финансирования. Автор заявляет об отсутствии внешнего финансирования при проведении исследования.

Конфликт интересов. Автор декларирует отсутствие явных и потенциальных конфликтов интересов, связанных с публикацией настоящей статьи.

Вклад авторов. Все авторы подтверждают соответствие своего авторства международным критериям ICMJE (все авторы внесли существенный вклад в разработку концепции, проведение исследования и подготовку статьи, прочли и одобрили финальную версию перед публикацией). Наибольший вклад распределён следующий образом: Кабдушев А.А. – написание и редактирование рукописи, Баймаханов А.Е. – интерпретация данных, Агзамов Ф.А – написание и редактирование рукописи, Дарибаев Ю.А. – сбор, анализ данных, концепция работы, Бетжанова А.Ж. – сбор, анализ данных, концепция работы.

ADDITIONAL INFORMATION

Funding source. This study was not supported by any external sources of funding.

Competing interests. The author declares no competing interests related to the publication of this article.

Authors’ contribution. All authors confirm the compliance of their authorship with the international ICMJE criteria (all authors made a substantial contribution to the conception of the work, acquisition, analysis, interpretation of data for the work, drafting and revising the work, final approval of the version to be published and agree to be accountable for all aspects of the work). The greatest contribution is distributed as follows: Arman A. Kabdushev ― writing and editing of the manuscript; Abilkassim Ye. Baymakhanov– interpretation of data; Farit A. Agzamov – writing and editing of a manuscript; Yuldashbay A. Daribayev – acquisition, data analysis, conception of the work; Aizhan Zh. Betzhanova – acquisition, data analysis, conception of the work.

Об авторах

Арман Арстангалиевич Кабдушев

Таразский региональный университет им. М.Х. Дулати

Автор, ответственный за переписку.
Email: arman-kz@mail.ru
ORCID iD: 0000-0003-3579-9054

PhD

Казахстан, Тараз

Абилкасим Елеусизович Баймаханов

Уфимский государственный нефтяной технический университет

Email: a.baimakhanov@clinal.kz

канд. техн. наук

Россия, Уфа

Фарит Акрамович Агзамов

Уфимский государственный нефтяной технический университет

Email: faritag@yandex.ru
ORCID iD: 0000-0001-5850-5261

докт. техн. наук

Россия, Уфа

Юлдашбай Абуевич Дарибаев

Таразский региональный университет им. М.Х. Дулати

Email: nur920318@mail.ru
ORCID iD: 0000-0003-1962-0966

канд. с.-х. наук

Казахстан, Тараз

Айжан Жарылкасыновна Бетжанова

Таразский региональный университет им. М.Х. Дулати

Email: betzhanova83@mail.ru
ORCID iD: 0000-0002-8276-8384
Тараз

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