scholarly journals RETROFITTING DESIGN OF HEAT EXCHANGER NETWORKS USING ASPEN-HYSYS: A CASE STUDY OF CRUDE OIL REFINING PROCESS

2021 ◽  
Vol 40 (1) ◽  
pp. 15-22
Author(s):  
Mohammed Hussein ◽  
Elzahid N.M ◽  
Ebrahim Esmail ◽  
Mamdouh Gadalla ◽  
Ibrahim Ashour
2021 ◽  
Author(s):  
Milan Kambič

The base of the final product is the base oil. The final product is ready for use and is a mixture of base oil (or several base oils) and additives. Additives improve the properties of the base oil. Base oils can be mineral or synthetic based. Base oils or base stocks are created from separating and cleaning up crude oil. They are one of several liquid components that are created from crude oil. The crude oil refining process will be briefly described. The American Petroleum Institute implemented a system for describing various base oil types. The result was the development and introduction of base oils group numbers. The API numbers of various base oil groups and the main differences between them will be explained. At the end, premium quality hydraulic oil and its main characteristics will be presented.


2015 ◽  
Vol 1107 ◽  
pp. 335-340 ◽  
Author(s):  
Nurasmat Mohd Shukri ◽  
Jafariah Jaafar ◽  
Wan Azelee Wan Abu Bakar ◽  
Zaiton Abdul Majid

An increasing interest in acidic fractions in crude oil was prompted by the corrosion problems that these compounds caused during oil refining process. This corrosion is associated with the total acid number (TAN). With the anticipated growth of acidic crudes in the market, a new technology for removal of the acidic fractions was introduced. Petronas Penapisan Melaka Light Crude (B) with TAN values of 2.52 was studied. The ammoniated polyethylene glycol (PEG) was used as the deacidifying agent in this study with a concentration range of 100-2500 mg/L. Data indicated that the optimal content of ammoniated polyethylene glycol in crude B was 1500 mg/L, and PEG with molecular weight of 2000 was the most promising co-solvent with the reagent/oil ratio being 0.4:1 (wt/wt). A reaction time of 5 min with a suitable reaction temperature of 40°C and optimal stirring time of 5 min were sufficient to achieve the goal for crude oil B. The TAN was lowered to 0.28 for crude oil B. The percentage of acid removal for crude B was 78. An increase in the concentration of basic chemical reduced the TAN value for crude oil B to less than 1.


Author(s):  
Ping Chen ◽  
Cong Luo

This paper describes an improved design of end closure for screw locking ring U-shaped tube heat exchanger used in oil-refining process with use of the D-section shearing bolts as its load-carrying connectors between the tube channel cover and the top flange instead of the connection by acme screw locking ring and the strength calculating method for its main load-carrying components and an comparison with two others are presented. This new construction has the features of compacted design, saving material and easy assembling and disassembling etc.


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