A System of Multistep Self-Learning Forecast and its Application on Oil Refining Industry

2012 ◽  
Vol 605-607 ◽  
pp. 1675-1678
Author(s):  
Jing Chen

The catalytic cracking unit of oil refining industry, is a complex process characterized by its prolonged time delay and strong coupling ability.This system adopts the method of modern control theory, artificial intelligence combined effectively production techniques, researchs the problem of the multistep self-learning experience forecast online by computers and its applications in oil refinery. The system guides and optimizes the operations of the production process based on its memory, comparisons and analysis. The system is very effective to increase yield; It has been applied and popularized in 20 large-scale or middle-scale oil refining corporations.

2019 ◽  
pp. 77-81
Author(s):  
E. A. Mishukov ◽  
Yu. N. Linnik

The current challenges of the domestic oil refining industry have been identified. The significance of the latest requirements for the quality of petrochemical products has been highlighted, as well as the need for technical and technological updating of oil refineries has been described. The use of the Nelson index as an assessment of the quality of petrochemical products at refineries has been considered. The formulas of the complexity factor and the Nelson index have been described. The principles and mechanisms of calculating the Nelson index for a conditional oil refinery have been disclosed. The statistics on the most modern oil refineries in Russia, using the Nelson index, has been presented. An analysis and comparison of changes by country within the framework of this indicator over the past years have been compiled.


2018 ◽  
Vol 11 (1) ◽  
pp. 113 ◽  
Author(s):  
Francesco Ferella ◽  
Idiano D’Adamo ◽  
Simona Leone ◽  
Valentina Innocenzi ◽  
Ida De Michelis ◽  
...  

Every year the oil refining industry consumes thousand tons of fluid catalytic cracking zeolite from the E-cat generated in the fluid catalytic cracking (FCC) unit. In the present paper, a new process for recycling of fluid catalytic cracking catalysts (FCCCs) is presented. The process, previously tested at laboratory scale, was simulated by SuperPro Designer catalysts (FCCCs, also known as equilibrium catalysts, E-cat), which are mainly landfilled. Their intrinsic value is quite low and the content of rare earth elements (REEs), as lanthanum and cerium oxides, is around 3%wt. Moreover, their reuse in other industrial processes as raw material is very scarce. For each metric ton of spent FCCC treated for recovery of REEs, nearly the same amount of waste is generated from the process, the majority of which is represented by the solid residue resulting from the leaching stage. The manuscript presents a technological study and an economic analysis for the recovery of REEs, as well as the production of synthetic © software package. The plant was designed for a capacity of 4000 metric tons per year. The discounted cash flow (DCF) method was applied and Net Present Value (NPV) equal to about two-million € and Discounted Payback Time (DPBT) equal to two years defined the profitability of the process for recycling of FCCCs. This result depends on the selling price of zeolite. Consequently, a break-even point (BEP) analysis was conducted on this critical variable and the condition of economic feasibility was verified with a price of 1070 €/ton. This study tried to implement recycling strategies towards circular economy models.


The success of the Program of housing stock renovation in Moscow depends on the efficiency of resource management. One of the main urban planning documents that determine the nature of the reorganization of residential areas included in the Program of renovation is the territory planning project. The implementation of the planning project is a complex process that has a time point of its beginning and end, and also includes a set of interdependent parallel-sequential activities. From an organizational point of view, it is convenient to use network planning and management methods for project implementation. These methods are based on the construction of network models, including its varieties – a Gantt chart. A special application has been developed to simulate the implementation of planning projects. The article describes the basic principles and elements of modeling. The list of the main implementation parameters of the Program of renovation obtained with the help of the developed software for modeling is presented. The variants of using the results obtained for a comprehensive analysis of the implementation of large-scale urban projects are proposed.


Author(s):  
I. V. Ginko ◽  
T. M. Sushinskaya ◽  
A. L. Rybina

Studies have been conducted to assess the impact of factors of the production environment on employees of the oil refinery ofJSC «Naftan». Significant differences with the comparison group on the indicators of SVT were revealed. Priority nosological forms of employees of the main group are identified.


Molecules ◽  
2021 ◽  
Vol 26 (8) ◽  
pp. 2289
Author(s):  
Haihui Fu ◽  
Yan Chen ◽  
Tingting Liu ◽  
Xuemei Zhu ◽  
Yufei Yang ◽  
...  

Fluid catalytic cracking (FCC) spent catalysts are the most common catalysts produced by the petroleum refining industry in China. The National Hazardous Waste List (2016 edition) lists FCC spent catalysts as hazardous waste, but this listing is very controversial in the petroleum refining industry. This study collects samples of waste catalysts from seven domestic catalytic cracking units without antimony-based passivation agents and identifies their hazardous characteristics. FCC spent catalysts do not have the characteristics of flammability, corrosiveness, reactivity, or infectivity. Based on our analysis of the components and production process of the FCC spent catalysts, we focused on the hazardous characteristic of toxicity. Our results show that the leaching toxicity of the heavy metal pollutants nickel, copper, lead, and zinc in the FCC spent catalyst samples did not exceed the hazardous waste identification standards. Assuming that the standards for antimony and vanadium leachate are 100 times higher than that of the surface water and groundwater environmental quality standards, the leaching concentration of antimony and vanadium in the FCC spent catalyst of the G set of installations exceeds the standard, which may affect the environmental quality of surface water or groundwater. The quantities of toxic substances in all spent FCC catalysts, except those from G2, does not exceed the standard. The acute toxicity of FCC spent catalysts in all installations does not exceed the standard. Therefore, we exclude “waste catalysts from catalytic cracking units without antimony-based passivating agent passivation nickel agent” from the “National Hazardous Waste List.”


Author(s):  
Luis Ivan Ruiz Flores ◽  
J. Hugo Rodri´guez Marti´nez ◽  
Guillermo D. Taboada ◽  
Javier Pano Jimenez

Nowadays the refining sector in Mexico needs to increase the quantity and quality of produced fuels by installing new process plants for gasoline and ultra low sulphur diesel. These plants require the provision of electricity and steam, among other services to function properly, which can be supplied by the power plants currently installed in each refinery through an expansion of their generation capacity. These power plants need to increase its production of electricity and steam at levels above their installed capacity, which involves the addition of new power generating equipment (gas or steam turbo-generators) as well as the raise of the electrical loads. Currently, the Mexican Petroleum Company (PEMEX) is planning to restructure their electrical and steam systems in order to optimally supply the required services for the production of high quality fuels. In this paper the present status of the original electrical power systems of the refineries is assessed and the electrical integration of new process plants in the typical schemes is analyzed. Also this paper shows the conceptual schemes proposed to restructure the electrical power system for two refineries and the strategic planning focused on implement the modifications required for the integration of new process plants that will demand about 20 MW for each refinery by 2014. The results of the analysis allowed to identify the current conditions of the electrical power systems in the oil refining industry or National Refining Industry (NRI), and thereby to offer technical solutions that could be useful to engineers facing similar projects.


2021 ◽  
Vol 66 (05) ◽  
pp. 106-108
Author(s):  
Aytac Turab qızı Hüseynova ◽  

The Oil Refinery of Heydar Aliyev was created in July 1953 as a new oil refining plant Baki. The combined atmospheric vacuum plant is the main plant at the oil refining factory and its starting capacity produces 6 million tons of crude oil. In 2010, 43,000 tons A-98, 1.18 tons of A-92 and 19,700 tons of gasoline A-80. At the same time, 600 400t kerosene, 214,000 diesel fuels, 214,000 tons. Liquid gas, 267 500t coke and 220 600t. With this investigation, the history of the oil refinery and the details of modernization were considered. 21 out of 24 types of Azerbaijani oil are processed at the Baku Oil Refinery named after Heydar Aliyev, of which 15 types of oil products, including gasoline, aviation kerosene, diesel fuel, fuel oil, petroleum coke, etc. are produced. The plant fully meets the needs of the republic in oil products. In addition, 45% of oil products are exported to foreign countries. Key words: Azerbaijani, oil, recycling, factory, modernization


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