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شبیه سازی واحد جداسازی و ریکاوری آمونیاک پتروشیمی لردگان تحت لایسنس Casale
Simulation of Ammonia Separation and Recovery Unit at LORDEGAN Pet. Co.
مهر ۲۴, ۱۴۰۳
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Simulation of CO2 Removal From Natural Gas with MEA (1)

Description

In addition to improving the existing processes for energy production and consumption, the increase in global demand for natural gas also requires pollution control. One of the most serious problems faced by technologies related to natural gas processes is the presence of large amounts of acid gases. which makes up about 40% of the gas output from the wells.

About 46/13 % of natural gas reservoirs in the world contain more than 10% H2S and about 9/26% of these reservoirs contain more than 10% CO2 gas. In this project, we will simulate the removal of carbon dioxide from natural gas with the help of MEA.

Several methods have been proposed to reduce the amount of acid gases in natural gas. Among them, we can mention chemical adsorption, physical adsorption, hybrid process, surface adsorption using a solid column and using a membrane. Among these methods, the adsorption of acid gases by a liquid solvent (chemical adsorption) is the most common method used in the gas sweetening industry.

Natural gas sweetening unit

Sweetening of Natural Gas

In the 1930s, alkanol amines were used for gas sweetening for the first time. And from that time until the 1970s, monoethanolamine (MEA) was the most used, but since the 1970s, due to the disadvantages of monoethanolamine. such as corrosion and solvent wastage, diethanolamine (DEA) replaced this amine.

Since the mid-1970s, methyl diethanolamine (MDEA) has been widely used in the gas industry due to its advantages such as the ability to selectively separate hydrogen sulfide in the presence of carbon dioxide. high stability, and low energy consumption for solvent recovery. Alkanol amines generally consist of at least one hydroxyl group (-COH) and at least one amino group (-NH2).

Conventional Amines Used in Sweetening Gas

Primary amines, Mono Ethanol Amine (MEA) and Di Glycol Amine (DGA)

Secondary amines, Di Ethanol Amine (DEA) and Di Iso Propanol Amine (DIPA)

Tertiary amines, Tri Ethanol Amine (TEA) and Methyl Di Ethanol Amine (MDEA)

Simulation of CO2 Removal From Natural Gas With MEA (1)

In this project, the natural gas sweetening unit is simulated with MEA in Aspen Hysys software. To buy the project or get more information about it, proceed through the link below.


Price: 103 $

 

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