1591. Increasing the processing capacity of vacuum distillation plants (for crude oil) utilizing a distillation-refining-redistillation scheme

Vacuum ◽  
1966 ◽  
Vol 16 (8) ◽  
pp. 473
2018 ◽  
Vol 196 ◽  
pp. 04038
Author(s):  
Eva Remišová ◽  
Michal Holý

In recent years, there has been a further development of refining technology, which make it possible to better use of crude oil, which also has a major impact on the quality of bitumen. Most European refineries, of course, are processing, for reasons of the resale of petroleum products, especially petroleums suitable for the recovery of light and middle fractions. Therefore, light petroleums are required, with low yields of heavy fractions, which are highly economically and in dispositions efficient for processors on the petroleum market. Emphasis is placed on the sulfur content, the paraffin content is no longer the most important aspect. Less important from the perspective of the refinery is the content and the ratio of asphaltenes and maltenes. There is no doubt that we will have to change our view on petroleum products. Their availability will continue to decline, their price, on the other hand, is likely to grow in relation to falling supplies of resources. Therefore, the view of the bitumen must be changed. The most common way of production of PG bitumen is vacuum distillation, which is carried out in such a way that the vacuum distillation residue satisfies it´s properties bitumen requirements for the relevant penetration.


2019 ◽  
Vol 103 ◽  
pp. 9-19 ◽  
Author(s):  
Jisheng Tian ◽  
Lida Wang ◽  
Wen Sun ◽  
Yong Yang ◽  
Zhimei Liu ◽  
...  

2009 ◽  
Vol 23 (12) ◽  
pp. 6015-6019 ◽  
Author(s):  
Juliana S. F. Pereira ◽  
Paola A. Mello ◽  
Fábio A. Duarte ◽  
Maria de Fátima P. Santos ◽  
Regina C. L. Guimarães ◽  
...  

2021 ◽  
Vol 1195 (1) ◽  
pp. 012050
Author(s):  
S X H’ng ◽  
L Y Ng ◽  
D K S Ng ◽  
V Andiappan

Abstract Crude oil blending is an important step for the operation of crude distillation systems in the refinery to improve the yield and profitability of the products. The product’s yield and quality are strongly dependent on the properties of the crude oil. However, the products of crude distillation units, especially the vacuum distillation unit (VDU) need to satisfy the yield and quality requirements of the downstream process units in the refinery. Otherwise, the performance of downstream processes will be affected, and loss of profitability in the refinery. Hence, it is important to optimise the performance of the VDU to ensure the optimum operation of VDU. This work covers the process simulation of VDU, surrogate modelling and mathematical optimisation model. The objective of the developed optimisation model is to determine an optimal for maximum high vacuum gas oil (HVGO) yield and minimum total annualised cost (TAC) respectively. To do this, crude oil blending ratio, column temperature, column pressure, stripping steam flowrate, pump-around flowrate in the VDU are optimised. Based on the optimised result, the heavy-light crude blend achieves higher HVGO yield and lower TAC as compared to the heavy-medium crude blend and heavy-medium-light crude blend. The optimised results can provide insight into the optimal process conditions of VDU for the refiners. With this insight, effective operating strategies can be developed to overcome the limitations present in real VDU operations.


2019 ◽  
Vol 13 (1) ◽  
pp. 7-22 ◽  
Author(s):  
Angela O. Mamudu ◽  
Ebenezer Okonkwo ◽  
Stephen I. Okocha ◽  
Emeka E. Okoro ◽  
Francis Elehinafe ◽  
...  

Objective: Generally, Petroleum refineries are put in place to convert or refine unprocessed crude oil into more useful products using both physical separation and chemical conversion processes. Albeit, different refining unit are subsets of the physical separation category. The atmospheric and vacuum distillation unit seems to be more prominent. Conventionally, the crude atmospheric residue cannot be further heated in an atmospheric condition due to: coke formation, pipes plugging, thermal cracking and straining of the furnace. A vacuum distillation column is therefore required. Methods: This study, therefore, focuses on the limitations, “over straining of the furnace to provide the necessary heat” and “non-reliance on the additional re-boiler since it only acts as a heat exchanger”. An integrated distillation column with a capacity of 10,000 barrel per day was therefore designed for the concurrent production of all distillate cuts. Results: This was achieved through the introduction of a submerged combustion zone at the stripping section of the column where Naphtha was utilized as the source of fuel. Verification of this approach was also conducted using Autodesk invention software and a finite element analysis tool to evaluate both thermal and computational fluid analysis impact. Overall, all derived distilled products met the American Society for Testing and Material Standard Table 6.


2013 ◽  
Vol 331 ◽  
pp. 21-24
Author(s):  
Zheng Fang Wang

Introduced the characters of crude oils containing sulfur and naphthenic acid, analyzed the corrosion and safety of this kind of oil acted on refinery equipment, investigated the corrosion on oil atmospheric and vacuum distillation equipment, delayed coking unit and gas desulphurization unit. Tabled a proposal to forecast life of the device using risk based inspection and grey system theory, assured the equipment to run long-term and safety.


Energy ◽  
2014 ◽  
Vol 76 ◽  
pp. 559-571 ◽  
Author(s):  
Wugen Gu ◽  
Yuqing Huang ◽  
Kan Wang ◽  
Bingjian Zhang ◽  
Qinglin Chen ◽  
...  

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