Кафедра "Видобування нафти, газу та конденсату"

Постійне посилання колекціїhttps://repository.kpi.kharkov.ua/handle/KhPI-Press/927

Офіційний сайт кафедри http://web.kpi.kharkov.ua/dngik

Кафедра "Видобування нафти, газу та конденсату" була заснована в 2010 році для підготовки спеціалістів в нафтогазовій промисловості.

Характерною рисою діяльності кафедри "Видобування нафти, газу та конденсату" є постійний зв'язок з підприємствами та організаціями-замовниками фахівців. Випускники кафедри працюють у галузі видобування, транспортування, використання та реалізації нафти і газу, а також великої кількості сировини, отриманої при їх технологічній переробці.

Кафедра входить до складу Навчально-наукового інституту хімічних технологій та інженерії Національного технічного університету "Харківський політехнічний інститут".

У складі науково-педагогічного колективу кафедри працюють: 2 доктора технічних наук, 3 кандидата технічних наук; 2 співробітника мають звання професора, 1 – доцента, 1 – старшого наукового співробітника.

Переглянути

Фільтри

2019 - 20202

Налаштування

ORCID: search.filters.orcid.https://orcid.org/0000-0001-7552-0236

Результати пошуку

Зараз показуємо 1 - 2 з 2
  • Ескіз
    Документ
    Improvement of an engineering procedure for calculating the non­isothermal transportation of a gas­liquid mixture
    (Технологический центр, 2019) Fyk, M. I.; Biletskyi, V. S.; Fyk, I.; Bondarenko, Volodymyr; Mohammed, Bassam Al-Sultan
    The study that we conducted into the process of transportation of a gas-condensate mixture from a well bottom to the separation production plant has revealed the features of isothermal and non-isothermal flow. It was proved that during non-isothermal flow, hydraulic losses in the product pipeline are significantly affected by throttle effect and energy accommodation effect. The influence of velocity and volumetric flow rate of the gas-liquid mixtures on hydraulic resistance and pressure drop on a section of product pipeline, taking into consideration non-isothermal flow was analyzed. It was found that the assessment of hydraulic resistance and pressure drop in the proposed dependences converges with standardized ones by 95 %. The result was obtained based on the developed system of equations of the mathematical model for non-isothermal non-stationary one-dimensional motion of the gas-liquid mixture of hydrocarbons in the pipeline. The proposed system beneficially differs from the known ones by the fact that it takes into consideration the inner convective heat exchange, estimated by the combined effect of Joule-Thomson. A distinctive feature of the improved procedure for calculation was the introduction of temperature correction and accommodation coefficient in the calculation of hydraulic resistance of a pipeline as a system with distributed parameters. Due to this, it became possible to improve the procedure for the calculation of non-isothermal transportation of a homogeneous gas-condensate mixture. Based on the analysis of calculation curves by the known procedures (formulas of Thomas Colebrooke, Leibenson and VNIIgas) for isothermal and non-isothermal processes and the proposed procedure, rational areas of their applications were shown. All calculations were performed at the velocity of a gas-liquid flow within the range 0–50 m/s, pipe roughness of 0.01–0.05 mm and their diameter of 100–300 mm, the data from actual production pipelines of Novotroitsk oil-gas condensate field were used. Comparison of the theoretical and industrial experiments showed sufficient for engineering practice accuracy of calculation of pressure drop on the stretches of oil and gas lead lines and allowed recommending the developed analytical dependences for the introduction in industrial engineering.
  • Ескіз
    Документ
    Mathematical simulation of heat and mass exchange processes during dissociation of gas hydrates in a porous medium
    (Національний гірничий університет, 2020) Dreus, A. Yu.; Bondarenko, V. I.; Biletskyi, V. S.; Lysenko, R. S.
    Purpose. The development of methodology of research and analysis of heat and mass exchange processes in a hydrate containing porous rock layer in case of a pressure drop at its boundary. Methodology. Mathematical simulation, computational experiment findings. The mathematical simulation of thermophysical processes during the dissociation of gas hydrate in a porous rock layer is presented. The case of gas hydrate dissociation in a porous rock layer, which exists in a stable state under the influence of relatively high initial temperature and pressure factors, is investigated. Numerical studies on the temperature and pressure patterns during the gas hydrate dissociation are performed. The nonstationary distribution of temperature and pressure along a porous rock layer during the dissociation of gas hydrate due to pressure drop at its boundary is presented. The advancement rate of the gas hydrate dissociation front and the change in the size of the dissociated gas hydrate area over the time are determined. originality. The algorithm is proposed for calculating the pressure and temperature fields in a porous rock layer in the case when the temperature of the stable gas hydrate is higher than its dissociation temperature. The factor that ensures the dissociation of gas hydrate is the pressure drop at the rock layer boundary. The effect of the endothermal reaction of gas hydrate dissociation on the heat exchange processes in the porous rock layer is presented. It is shown that the temperature and pressure values determining the gas hydrate dissociation point are changed as the front of the phase transition advances. Practical value. The proposed mathematical model and calculation algorithm can be used to predict the time characteristics and sizes of the gas hydrate dissociation zones around production wells.