STUDY OF THE EFFECTIVE FACTORS IN GASOLINE SWEETENING PROCESS (original) (raw)

Advanced Control Solution for a Refinery Gas Sweetening Process

Revista de Chimie

Gas sweetening unit, also known as acid gas removal unit, is a wide used unit in refineries and petrochemical plants and refers to a group of processes that use different amines such DiEthanolAmine (DEA) to remove the hydrogen sulfide (H2S) from gases, in order to use them as fuel to different furnaces from other processing units. If the hydrogen sulfide is not well removed, will lead to furnaces tubular corrosion and therefore will generate loss in refractory properties. Also, the emission values of the exhaust gases will not be in accordance with the environmental regulations. The paper outlines the main results obtained by authors concerning the advanced control solution for a refinery gas sweetening unit and contains three parts. The first part outlines the results of the dynamic gas sweetening process investigation using HYSYS� simulation software. The second part presents the proposed structure of the advanced control system and the third part outlines the results obtained usi...

Simulation of hydrodesulfurization unit for natural gas condensate with high sulfur content

The natural gas condensates are composed of various components of hydrocarbons and some contaminants such as hydrogen sulfide, thiols (mercaptans), and aromatics. Thus, the natural gas condensates could be considered as a fuel resource. This study concerned the simulation of an Ultra-Deep Hydrodesulfurization (UDHDS) unit plus a distillation section to treat a combination of gas condensate and disulfide oils (DSO) and produce clean fuel cuts. Gas condensate of South Pars field of Iran with high sulfur content was applied to obtain clean fuel cuts. In order to reduce the sulfur content of this stream to less than 10 ppmw as sulfur, a UDHDS unit was simulated using Aspen HYSYS software package. The clean gas condensate leaving the UDHDS unit (with sulfur content \10 ppmw) contains complex mixtures of hydrocarbon components called petroleum cuts which are identified by their boiling points ranges. To obtain the narrow fractions of butane, light naphtha, heavy naphtha, kerosene, and gasoil, a fractional distillation system was simulated. The simulation results revealed that the top products of distillation column, namely butane, light naphtha, and heavy naphtha were sulfur free and the sulfur contents of kerosene and gasoil cuts were 12 and 27 ppmw as sulfur, respectively.

Modelling and Simulation of Methanol and Biodiesel Production Processes Using Innovative Technologies

Chemical Engineering Transactions, 2020

Biodiesel is considered to be a promising alternative or additive to fossil fuel. Biodiesel, fatty acid methyl esters (FAME), is produced by transesterification of triglycerides or fatty acids with alcohols (i.e. methanol or ethanol, in the presence of a suitable acidic or alkaline catalyst. The present work is focused on process modelling and simulation of biodiesel production using: i) an innovative method for methanol synthesis, methanol being an important raw-material for biodiesel, as well as ii) an intensified method for biodiesel production (i.e. reactive distillation – RD). Methanol production from CO2 and H2 is considered to be an interesting method for CO2 utilization. The main advantages of this method are the reduction of greenhouse gas emissions and the production of one valuable chemical, methanol. The H2 for the methanol synthesis is obtained from wood chips through chemical-looping gasification. Beside methanol, other raw-materials for biodiesel production are trigly...

On-Line Optimization, Energy Analysis and Environmental Impact Assessment of Sulfuric Acid Catalyzed Alkylation Process

2003

An Advanced Process Analysis System was successfully applied to the 15,000 BPD alkylation plant at the Motiva Enterprises Refinery in Convent, Louisiana. Using the flowsheeting, on-line optimization, pinch analysis, and pollution assessment capabilities of the System (Telang et al., 1999) a significant increase in profit and energy savings were projected through reduced steam usage in the distillation columns. A small decrease in sulfuric acid consumption potentially could be obtained. 1. Introduction Alkylation process is one of the most important refinery processes for producing conventional gasoline. Alkylation offers several key advantages to refiners, including the highest average quality of all components available to the gasoline pool, increased amounts of gasoline per volume of crude oil and high heats of combustion. The overall process is a composite of complex reactions, and consequently rigorous control is required of operating conditions and of catalyst to assure predict...