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AUTOMATED SYSTEM FOR MONITORING THE GAS CONTENT AND PARAMETERS OF TEMPORARY SEALING DEVICES ON MAIN GAS PIPELINES 监测主输气管道临时密封装置气体含量和参数的自动化系统
Pub Date : 2024-04-17 DOI: 10.17122/ogbus-2024-2-130-140
Eliza N. Yakhina, Gulnara M. Sharafutdinova
Control of the gas transportation process is the main direction in the operation of gas pipelines. The main specificity of the operating conditions of control systems lies in their geographical location along the main gas pipelines. As a rule, the facilities in operation are at a considerable distance from the control points, so automation should be used to control several parameters in the gas pipelines. The control of gas contamination is a complex and responsible process, the aim of which is to detect and prevent possible gas leaks that could lead to negative consequences, including fires, explosions and pollution. Continuous air monitoring includes monitoring and analysis of air composition for harmful substances. This makes it possible to quickly determine the presence and concentration of hazardous substances in the air and to take measures to prevent and minimize their impact on workers, as well as to create healthy health and hygiene conditions for staff.The article is devoted to the safety control system, which is designed to provide an automated continuous control over the gas-air medium and parameters of temporary sealing devices during work on the linear part of the main gas pipeline. Its application makes it possible to increase the level of safe working conditions of employees during work on main gas pipelines by reducing the probability of occurrence of accidents and related losses.
天然气运输过程的控制是天然气管道运行的主要方向。控制系统运行条件的主要特殊性在于其沿主要天然气管道的地理位置。通常情况下,运行中的设施距离控制点有相当大的距离,因此应使用自动化控制天然气管道中的多个参数。气体污染控制是一个复杂而又责任重大的过程,其目的是检测和防止可能导致火灾、爆炸和污染等不良后果的气体泄漏。连续空气监测包括监测和分析空气中有害物质的成分。这使得快速确定空气中有害物质的存在和浓度成为可能,并采取措施防止和尽量减少有害物质对工人的影响,同时为员工创造健康卫生的条件。本文专门介绍安全控制系统,该系统的设计目的是在主输气管线性部分施工期间对气体-空气介质和临时密封装置的参数进行自动连续控制。该系统的应用可降低事故发生概率和相关损失,从而提高员工在主要天然气管道工作期间的安全工作条件水平。
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引用次数: 0
PHYSICAL AND CHEMICAL PROPERTIES OF OIL FRACTIONS FROM GAS CONDENSATE OF AL-MASILA FIELDS (REPUBLIC OF YEMEN) Al-Masila 油田(也门共和国)天然气凝析油馏分的物理和化学特性
Pub Date : 2024-03-06 DOI: 10.17122/ogbus-2024-1-161-175
Ahmed Taha Abdullah Galeb Saleh, A. T. Gilmutdinov, I. G. Lapshin
The results of physical and chemical studies of gas condensate fractions, including gasoline, kerosene and diesel, are presented. Experiments were carried out on the separation of gasoline, kerosene and diesel fuel from gas condensate into fractions. The analysis showed that the collected gas condensate contains 38.02 % gasoline with a boiling point of 180 °C, 20.87 % kerosene with a boiling point of 140–240 °C and 43.67 % diesel fuel with a boiling point of 180–360 °C. The 140–240 °C fraction was obtained by secondary distillation of the straight-run fraction. The data obtained confirm that these fractions are high-quality raw materials for the production of motor gasoline, diesel fuel and jet fuel that meet modern standards. As a result of physical and chemical studies, the properties of the above mentioned fractions and their potential in the production of commercial petroleum products were determined.
本文介绍了天然气凝析油馏分(包括汽油、煤油和柴油)的物理和化学研究结果。实验将汽油、煤油和柴油从气体冷凝液中分离出来。分析表明,收集的气体冷凝液中含有 38.02 % 的汽油(沸点为 180 ℃)、20.87 % 的煤油(沸点为 140-240 ℃)和 43.67 % 的柴油(沸点为 180-360 ℃)。140-240 °C 的馏分是通过对直馏馏分进行二次蒸馏得到的。获得的数据证实,这些馏分是生产符合现代标准的车用汽油、柴油和喷气燃料的优质原料。通过物理和化学研究,确定了上述馏分的特性及其生产商业石油产品的潜力。
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引用次数: 0
CYBER SECURITY FOR INDUSTRIAL AUTOMATION & CONTROL SYSTEMS 工业自动化和控制系统的网络安全
Pub Date : 2024-03-06 DOI: 10.17122/ogbus-2024-1-176-194
Subramaniam Janakiraman
Cyber Security is an increasingly important subject while designing an Industrial Automation and Control System (IACS). IACS carries lot of data regarding a facility – Offshore production platform, process platform, Onshore Refinery, Petrochemical, Chemical plant etc. These data are very important to the end-users and stake holders in terms of assessment of production rate, quality of the produce, pros and cons in maintaining the facility, sales, profits and losses, future plans etc.This write-up provides an insight into the following topics:• What is a Cyber Security?• Types of Cyber Security• Why is Cyber Security important to industry?• Ways to implement Cyber Security – for IACS• Applicable Industry Standards – for IACS• CAPEX and OPEX involved• Management of Cyber Security Package• Conclusion
在设计工业自动化与控制系统(IACS)时,网络安全是一个日益重要的课题。IACS 承载着有关设施的大量数据--海上生产平台、工艺平台、陆上炼油厂、石化厂、化工厂等。这些数据对于最终用户和利益相关者评估生产率、产品质量、维护设施的利弊、销售、盈亏、未来计划等都非常重要。本文将深入探讨以下主题:- 什么是网络安全?- 网络安全的类型- 为什么网络安全对工业非常重要?
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引用次数: 0
MANAGING SAFETY CULTURE AS A WAY TO REDUCING INJURIES AT AN ENTERPRISE 将安全文化管理作为减少企业伤害的一种方式
Pub Date : 2024-03-06 DOI: 10.17122/ogbus-2024-1-53-74
Svetlana V. Onopenko, Maksim V. Prosin, Irina M. Ugarova, Anastasia S. Ushakova, Natalya N. Turova, E. I. Stabrovskaya
The article discusses issues of safety culture as a way to reduce injuries. The situation of industrial safety in Russia over the past few years, statistics of industrial injuries in different countries of the world are considered. Shown are statistics of fatal work injuries per 100 thousand workers. The main causes of industrial injuries and accidents are given. A survey was conducted to find out whether employees adhere to the safety culture. Based on the survey results, a method was proposed to reduce injuries at the enterprise. Organizational methods and techniques for improving safety culture are proposed.
文章讨论了安全文化作为减少伤害的一种方式的问题。文章介绍了过去几年俄罗斯的工业安全状况以及世界各国的工伤统计数据。文章列出了每 10 万名工人中致命工伤的统计数据。还给出了工伤和事故的主要原因。进行了一项调查,以了解员工是否遵守安全文化。根据调查结果,提出了减少企业工伤的方法。提出了改进安全文化的组织方法和技术。
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引用次数: 0
OPTIMIZATION OF THE CONDENSATE PUMPING SYSTEM AT THE GASOLINE SELECTIVE HYDROTREATING PLANT 优化汽油选择性加氢处理厂的凝析油泵系统
Pub Date : 2024-03-06 DOI: 10.17122/ogbus-2024-1-149-160
Vitaliy S. Lavrentev, Bulat R. Makhmudov, Vera V. Fomina, Dmitriy A. Kuvaitsev, Nikita S. Zatylkin, Sergey V. Anpilogov
The article discusses issues related to energy saving of the coolant – high, medium and low pressure water vapor in the condensate pumping system at the gasoline selective hydrotreating plant. The analysis of the current condensate pumping system is carried out and its main disadvantages are indicated. Retrofitting of the pumping system is proposed. A return line has been added and a pair of centrifugal pumps has been included in the technological scheme, a calculation has been made. The replacement of the equipment will optimize the steam consumption inside the gasoline selective hydrotreating plant and will reduce the cost of repair and maintenance of the unit, as well as electricity consumed for technological needs.
文章讨论了汽油选择性加氢处理厂冷凝液泵系统中冷却剂--高、中、低压水蒸气的节能问题。文章对当前的冷凝液泵系统进行了分析,并指出了其主要缺点。建议对泵系统进行改造。在技术方案中增加了一条回流管线和一对离心泵,并进行了计算。更换设备将优化汽油选择性加氢处理装置内的蒸汽消耗,降低装置的维修和维护成本,以及技术所需的电力消耗。
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引用次数: 0
REGULATORY REQUIREMENTS FOR CALCULATING FIRE RISK AND ACCIDENTS AT HAZARDOUS PRODUCTION FACILITIES AND THE IMPACT OF FIRE EXTINGUISHER USE ON THE CALCULATIONS 计算危险生产设施火灾风险和事故的法规要求,以及灭火器的使用对计算的影响
Pub Date : 2024-03-06 DOI: 10.17122/ogbus-2024-1-6-17
F. Khafizov, I. K. Bakirov, Liliya H. Zaripova, Inna V. Ozden, Tatyana V. Latypova
With the entry into force in 2009 of Federal Law No. 123-FZ «Technical Regulations on Fire Safety Requirements», fire risk assessment, fire audit and the development of fire safety declarations have become more relevant. The provision of the object of protection with primary fire extinguishing means, namely fire extinguishers, has a great influence on the value of fire risk.In this article, the use of fire extinguishers in case of accidents at hazardous production facilities is studied, measures and ways to solve emerging problems associated with the lack of additional research and field tests are proposed.
随着 2009 年第 123-FZ 号联邦法《消防安全要求技术条例》的生效,火灾风险评估、消防审核和消防安全声明的制定变得更加重要。为保护对象提供主要灭火手段(即灭火器)对火灾风险值有很大影响。本文研究了危险生产设施发生事故时灭火器的使用情况,提出了解决与缺乏额外研究和现场试验有关的新问题的措施和方法。
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引用次数: 0
OXIDATIVE REGENERATION OF METAL COMPLEX CATALYTIC SYSTEM 金属复合物催化系统的氧化再生
Pub Date : 2024-03-06 DOI: 10.17122/ogbus-2024-1-131-148
S. R. Sakhibgareev, A. D. Badikova, Mikhail A. Tsadkin, Ivan M. Borisov, I. N. Kulyashova, Margarita R. Sultanova
When carrying out thermocatalytic destruction of hydrocarbon feedstock, catalysts are deactivated due to the formation of surface coke, which blocks active centers. In order to restore their previous activity and selectivity, as well as extend their service life, a process of catalyst regeneration is carried out. One of the effective methods for restoring the original activity of deactivated catalysts is oxidative regeneration, which is based on the oxidation of coke deposits on the surface of the catalyst.The article examines the dependences of the formation of surface coke when varying the temperature regime of the process from 450 °C to 550 °C during the thermocatalytic destruction of heavy petroleum feedstock – West Siberian oil fuel oil in the presence of a new metal complex catalytic system, where the active component is a chloroferrate complex (NaFeCl4 or TCFN) in an amount 10 %, deposited on a carrier, which is a deeply decationized Ymmm zeolite of the acidic form (H-form). The patterns of oxidative regeneration of a metal-complex catalytic system were studied by distilling off highly volatile products in a flow of inert gas (helium) and oxygen-containing gas.During the experiments, it was found that with an increase in the temperature of the thermocatalytic destruction process from 450 °C to 550 °C, a slight increase in coarse deposits on the surface of the catalyst was observed from 2,6 % wt. up to 3,5 % wt. respectively. When carrying out the process of oxidative regeneration of a carbonized catalyst with air oxygen (in a flow of helium) at a temperature of 500 °C for 60 min only volatile components are initially removed, and further calcination takes up to 180 min allows for complete burning of surface coke.
在对碳氢化合物原料进行热催化破坏时,催化剂会因表面焦炭的形成而失活,焦炭会阻塞活性中心。为了恢复催化剂以前的活性和选择性,并延长其使用寿命,需要进行催化剂再生处理。氧化再生是恢复失活催化剂原有活性的有效方法之一,它以催化剂表面沉积的焦炭氧化为基础。文章研究了在新型金属络合催化体系存在下对重质石油原料--西西伯利亚石油燃料油进行热催化破坏过程中,当工艺温度从 450 °C 变化到 550 °C 时表面焦炭形成的相关性,该催化体系的活性组分是氯铁酸酯络合物(NaFeCl4 或 TCFN),含量为 10%,沉积在载体上,载体是酸性形式(H-form)的深度分解 Ymmm 沸石。通过在惰性气体(氦气)和含氧气体流中蒸馏出高挥发性产物,研究了金属络合催化系统的氧化再生模式。在实验过程中发现,随着热催化破坏过程的温度从 450 °C 提高到 550 °C,催化剂表面的粗沉积物略有增加,分别从 2.6 % 重量比增加到 3.5 % 重量比。在 500 °C 的温度下,用空气氧气(在氦气流中)对碳化催化剂进行 60 分钟的氧化再生过程,最初只去除挥发性成分,进一步煅烧需要 180 分钟才能完全燃烧表面焦炭。
{"title":"OXIDATIVE REGENERATION OF METAL COMPLEX CATALYTIC SYSTEM","authors":"S. R. Sakhibgareev, A. D. Badikova, Mikhail A. Tsadkin, Ivan M. Borisov, I. N. Kulyashova, Margarita R. Sultanova","doi":"10.17122/ogbus-2024-1-131-148","DOIUrl":"https://doi.org/10.17122/ogbus-2024-1-131-148","url":null,"abstract":"When carrying out thermocatalytic destruction of hydrocarbon feedstock, catalysts are deactivated due to the formation of surface coke, which blocks active centers. In order to restore their previous activity and selectivity, as well as extend their service life, a process of catalyst regeneration is carried out. One of the effective methods for restoring the original activity of deactivated catalysts is oxidative regeneration, which is based on the oxidation of coke deposits on the surface of the catalyst.\u0000The article examines the dependences of the formation of surface coke when varying the temperature regime of the process from 450 °C to 550 °C during the thermocatalytic destruction of heavy petroleum feedstock – West Siberian oil fuel oil in the presence of a new metal complex catalytic system, where the active component is a chloroferrate complex (NaFeCl4 or TCFN) in an amount 10 %, deposited on a carrier, which is a deeply decationized Ymmm zeolite of the acidic form (H-form). The patterns of oxidative regeneration of a metal-complex catalytic system were studied by distilling off highly volatile products in a flow of inert gas (helium) and oxygen-containing gas.\u0000During the experiments, it was found that with an increase in the temperature of the thermocatalytic destruction process from 450 °C to 550 °C, a slight increase in coarse deposits on the surface of the catalyst was observed from 2,6 % wt. up to 3,5 % wt. respectively. When carrying out the process of oxidative regeneration of a carbonized catalyst with air oxygen (in a flow of helium) at a temperature of 500 °C for 60 min only volatile components are initially removed, and further calcination takes up to 180 min allows for complete burning of surface coke.","PeriodicalId":19570,"journal":{"name":"Oil and Gas Business","volume":"75 11","pages":""},"PeriodicalIF":0.0,"publicationDate":"2024-03-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140261256","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
SYNTHESIS OF MONOALKYL(C8-C12)PHENOLFORMALDEHYDE OLIGOMERS MODIFIED WITH IMIDAZOLINES AND AMIDAOAMINES BASED ON NATURAL PETROLEUM ACIDS AND POLYAMINES 以天然石油酸和多胺为基础,用咪唑和脒胺修饰的单烷基(c8-c12)酚醛低聚物的合成
Pub Date : 2024-03-06 DOI: 10.17122/ogbus-2024-1-89-104
M. N. Amiraslanova, Shakhla R. Aliyeva, P. E. Isayeva, N. Abdullayeva, R. A. Rustamov, F.A. Mammadzada, Saida F. Akhmedbekova
Monoalkyl(C8-C12)phenol-formaldehyde oligomers modified with imidazolines and amidoamines based on natural petroleum acids and polyamines have been synthesized. Diethylenetriamine, triethylenetetraamine, polyethylenepolyamines were used as amine compounds in obtaining nitrogen-containing modifiers. The component and quantitative composition of monoalkyl(C8-C12)phenol-formaldehyde oligomers modified with imidazolines and amidoamines of various compositions, the conditions for their preparation are given. The significance of the conducted research is substantiated.
以天然石油酸和多胺为基础,合成了用咪唑和氨基胺改性的单烷基(C8-C12)苯酚甲醛低聚物。二乙烯三胺、三乙烯四胺、多乙烯多胺被用作获得含氮改性剂的胺类化合物。给出了用咪唑和氨基胺改性的各种单烷基(C8-C12)苯酚-甲醛低聚物的组分和定量组成及其制备条件。证实了所进行研究的意义。
{"title":"SYNTHESIS OF MONOALKYL(C8-C12)PHENOLFORMALDEHYDE OLIGOMERS MODIFIED WITH IMIDAZOLINES AND AMIDAOAMINES BASED ON NATURAL PETROLEUM ACIDS AND POLYAMINES","authors":"M. N. Amiraslanova, Shakhla R. Aliyeva, P. E. Isayeva, N. Abdullayeva, R. A. Rustamov, F.A. Mammadzada, Saida F. Akhmedbekova","doi":"10.17122/ogbus-2024-1-89-104","DOIUrl":"https://doi.org/10.17122/ogbus-2024-1-89-104","url":null,"abstract":"Monoalkyl(C8-C12)phenol-formaldehyde oligomers modified with imidazolines and amidoamines based on natural petroleum acids and polyamines have been synthesized. Diethylenetriamine, triethylenetetraamine, polyethylenepolyamines were used as amine compounds in obtaining nitrogen-containing modifiers. The component and quantitative composition of monoalkyl(C8-C12)phenol-formaldehyde oligomers modified with imidazolines and amidoamines of various compositions, the conditions for their preparation are given. The significance of the conducted research is substantiated.","PeriodicalId":19570,"journal":{"name":"Oil and Gas Business","volume":"42 9","pages":""},"PeriodicalIF":0.0,"publicationDate":"2024-03-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140261660","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
LOW-TONNAGE METHANOL PRODUCTION PLANT IN FIELD CONDITIONS 田间低吨位甲醇生产装置
Pub Date : 2024-03-06 DOI: 10.17122/ogbus-2024-1-195-237
Yu. V. Zagashvili, Aleksey M. Kuzmin, Vasily N. Efremov
The concept of a low-tonnage methanol production plant in field production conditions is presented. The developed small-sized transportable installation ensures safety, reliability and maintainability in operation with a base capacity of 5,000 t of raw methanol per year. The technological process consists of two main stages: first, synthesis gas is obtained by partial oxidation of the prepared natural gas with air, and then synthesis gas is fed into a multi-reactor cascade of the methanol synthesis complex. The main apparatus of the installation is a domestic three-component (natural gas – air – chemically treated water) synthesis gas generator (SGG), which includes: mixing head, ignition device, combustion chamber, water injection unit, evaporation chamber. The technological complex of synthesis gas with SGG binding is described, the dimensions, parameters and performance of SGG are indicated, data from numerical modeling of partial oxidation of natural gas to obtain nitrogen-ballasted synthesis gas for the synthesis of methanol are presented. A simplified technological complex for the synthesis of methanol has been developed, which includes a direct-flow multi-reactor cascade with the release of raw methanol after each reactor, and numerical modeling of the cascade of synthesis of raw methanol has been carried out. As a result of the research, the degrees of conversion of carbon oxides into methanol were determined, which made it possible to assess the need for application of a three-reactor cascade with a degree of conversion up to 60 % and with a specific capacity of about 800–900 kg/h of raw methanol per 1000 nm3/h of natural gas. Experimental laboratory data are presented, which coincide with the calculations of the material balances of the installation devices.
介绍了野外生产条件下低吨位甲醇生产装置的概念。所开发的小型可运输装置可确保运行的安全性、可靠性和可维护性,基本产能为每年 5000 吨原料甲醇。技术流程包括两个主要阶段:首先,通过用空气对制备好的天然气进行部分氧化获得合成气,然后将合成气送入甲醇合成联合装置的多反应器级联。装置的主要设备是家用三组分(天然气-空气-化学处理水)合成气发生器(SGG),包括:混合头、点火装置、燃烧室、注水装置、蒸发室。介绍了与 SGG 结合的合成气技术综合体,说明了 SGG 的尺寸、参数和性能,并提供了天然气部分氧化以获得用于合成甲醇的氮压合成气的数值模拟数据。开发了一个简化的甲醇合成技术综合体,其中包括一个直流多反应器级联,在每个反应器之后释放原料甲醇,并对合成原料甲醇的级联进行了数值建模。研究结果确定了碳氧化物转化为甲醇的程度,从而可以评估是否需要采用转化率高达 60%、每 1000 nm3/h 天然气可生产约 800-900 kg/h 原料甲醇的三反应器级联技术。实验数据与安装设备的物料平衡计算相吻合。
{"title":"LOW-TONNAGE METHANOL PRODUCTION PLANT IN FIELD CONDITIONS","authors":"Yu. V. Zagashvili, Aleksey M. Kuzmin, Vasily N. Efremov","doi":"10.17122/ogbus-2024-1-195-237","DOIUrl":"https://doi.org/10.17122/ogbus-2024-1-195-237","url":null,"abstract":"The concept of a low-tonnage methanol production plant in field production conditions is presented. The developed small-sized transportable installation ensures safety, reliability and maintainability in operation with a base capacity of 5,000 t of raw methanol per year. The technological process consists of two main stages: first, synthesis gas is obtained by partial oxidation of the prepared natural gas with air, and then synthesis gas is fed into a multi-reactor cascade of the methanol synthesis complex. The main apparatus of the installation is a domestic three-component (natural gas – air – chemically treated water) synthesis gas generator (SGG), which includes: mixing head, ignition device, combustion chamber, water injection unit, evaporation chamber. The technological complex of synthesis gas with SGG binding is described, the dimensions, parameters and performance of SGG are indicated, data from numerical modeling of partial oxidation of natural gas to obtain nitrogen-ballasted synthesis gas for the synthesis of methanol are presented. A simplified technological complex for the synthesis of methanol has been developed, which includes a direct-flow multi-reactor cascade with the release of raw methanol after each reactor, and numerical modeling of the cascade of synthesis of raw methanol has been carried out. As a result of the research, the degrees of conversion of carbon oxides into methanol were determined, which made it possible to assess the need for application of a three-reactor cascade with a degree of conversion up to 60 % and with a specific capacity of about 800–900 kg/h of raw methanol per 1000 nm3/h of natural gas. Experimental laboratory data are presented, which coincide with the calculations of the material balances of the installation devices.","PeriodicalId":19570,"journal":{"name":"Oil and Gas Business","volume":"134 6","pages":""},"PeriodicalIF":0.0,"publicationDate":"2024-03-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140078458","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
STAGES OF ACCUMULATION OF OIL DROPLETS AND GAS BUBBLES IN THE DOME FOR CASES OF DEEP-SEA SPILLS: PART 2 深海泄漏情况下穹顶内油滴和气泡的积累阶段:第 2 部分
Pub Date : 2024-03-06 DOI: 10.17122/ogbus-2024-1-34-52
S. R. Kildibaeva, Maxim V. Stolpovsky
In a previously published article, the problem of mathematical modeling of the operation and installation of a special device – a separator dome designed to collect hydrocarbons for cases of deep-sea leaks was given, three initial stages of modeling the installation of the device were described. This paper describes in detail the remaining stages of installing the dome: the accumulation of a layer of gas, the final stage of installing the dome, when the tubes for pumping oil and gas are connected to the device and the device begins to work in stationary mode. Let's take a closer look at each of the stages. The fourth stage of the dome installation is associated with the achievement of a given height (at which the gas bubbles have not yet passed into the hydrate state) and the beginning of the migration of gas bubbles inside the dome. First, the gas bubbles migrate into layer of liquid immiscible with water, then in the oil layer. During this process, all the gas coming from the jet completely enters the tank. At the fifth stage, gas accumulations inside the tank are considered. At the sixth stage, the study of the accumulation of layers of gas and oil continues, but at the same time the reservoir itself sinks to the bottom of the reservoir at a constant speed. This is necessary to subsequently secure the dome and prevent oil and gas from leaking out of the dome. The seventh stage is the final one. At this stage, we believe that the dome is fixed on the ocean floor, pipes for pumping oil and gas are connected to it. As a result of the created mathematical model of the dome-separator operation, dependences characterizing the process of installation and functioning of the dome, the temperature dependences of gas and oil layers accumulated inside the dome, as well as the dynamics of accumulation of the corresponding layers in the dome are obtained. The characteristic start and end times of each of the stages are described.
在之前发表的一篇文章中,给出了一种特殊装置(用于收集深海泄漏情况下的碳氢化合物的分离穹顶)的运行和安装的数学建模问题,并描述了该装置安装建模的三个初始阶段。本文详细描述了安装穹顶的其余阶段:气体层的积累、安装穹顶的最后阶段(将抽取油气的管道连接到设备上,设备开始以静止模式工作)。让我们来详细了解每个阶段。穹顶安装的第四阶段与达到给定高度(此时气泡尚未进入水合物状态)和气泡开始在穹顶内迁移有关。首先,气泡进入与水不溶的液体层,然后进入油层。在此过程中,从喷射口喷出的所有气体完全进入油箱。第五阶段,考虑油箱内的气体积聚。在第六阶段,继续研究气层和油层的积聚,但同时储油罐本身以恒定的速度沉入储油罐底部。这是随后固定穹顶和防止油气从穹顶泄漏所必需的。第七阶段是最后阶段。在这一阶段,我们认为穹顶已固定在海底,用于抽取石油和天然气的管道与之相连。根据所建立的穹顶分离器运行数学模型,可以得出穹顶安装和运行过程的相关特性、穹顶内积聚的气层和油层的温度相关性以及穹顶内相应油层的积聚动态。对每个阶段的开始和结束时间进行了描述。
{"title":"STAGES OF ACCUMULATION OF OIL DROPLETS AND GAS BUBBLES IN THE DOME FOR CASES OF DEEP-SEA SPILLS: PART 2","authors":"S. R. Kildibaeva, Maxim V. Stolpovsky","doi":"10.17122/ogbus-2024-1-34-52","DOIUrl":"https://doi.org/10.17122/ogbus-2024-1-34-52","url":null,"abstract":"In a previously published article, the problem of mathematical modeling of the operation and installation of a special device – a separator dome designed to collect hydrocarbons for cases of deep-sea leaks was given, three initial stages of modeling the installation of the device were described. This paper describes in detail the remaining stages of installing the dome: the accumulation of a layer of gas, the final stage of installing the dome, when the tubes for pumping oil and gas are connected to the device and the device begins to work in stationary mode. Let's take a closer look at each of the stages. The fourth stage of the dome installation is associated with the achievement of a given height (at which the gas bubbles have not yet passed into the hydrate state) and the beginning of the migration of gas bubbles inside the dome. First, the gas bubbles migrate into layer of liquid immiscible with water, then in the oil layer. During this process, all the gas coming from the jet completely enters the tank. At the fifth stage, gas accumulations inside the tank are considered. At the sixth stage, the study of the accumulation of layers of gas and oil continues, but at the same time the reservoir itself sinks to the bottom of the reservoir at a constant speed. This is necessary to subsequently secure the dome and prevent oil and gas from leaking out of the dome. The seventh stage is the final one. At this stage, we believe that the dome is fixed on the ocean floor, pipes for pumping oil and gas are connected to it. As a result of the created mathematical model of the dome-separator operation, dependences characterizing the process of installation and functioning of the dome, the temperature dependences of gas and oil layers accumulated inside the dome, as well as the dynamics of accumulation of the corresponding layers in the dome are obtained. The characteristic start and end times of each of the stages are described.","PeriodicalId":19570,"journal":{"name":"Oil and Gas Business","volume":"11 3","pages":""},"PeriodicalIF":0.0,"publicationDate":"2024-03-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"140261957","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":0,"RegionCategory":"","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
引用次数: 0
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Oil and Gas Business
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