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World’s First | Introduction to Yangzi Petrochemical’s Naphtha Adsorption Separation Unit (MaxEne)

2017-03-01View Original

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Naphtha is one of the petroleum products, also known as light oil for chemical use. It is a lightweight oil produced by processing crude oil or other raw materials and is used as a raw material in the chemical industry, primarily for reformation and other chemical processes. There are various boiling ranges depending on the application; in China, the boiling range is defined as from the initial boiling point up to around 220°C. When used as a reforming feedstock for the production of aromatics, the fraction ranging from 70°C to 145°C is referred to as light naphtha ; When the goal is to produce high-octane gasoline, fractions ranging from 70°C to 180°C are used, along with weighed naphtha ; When used as a solvent, it is called solvent naphtha ; Aromatic solvents derived from coal tar are also known as heavy naphtha or solvent naphtha. Refining and petrochemical companies have traditionally used naphtha to produce gasoline, aromatics, as well as light olefins such as ethylene and propylene. Naphtha is primarily composed of n-paraffins, isoparaffins, cycloparaffins, and aromatics, and different applications require varying compositions of hydrocarbons in naphtha. Under normal circumstances, n-alkanes are the ideal feedstocks for steam cracking to produce ethylene ; For reformation feedstocks, naphthenes and aromatics are ideal materials ; Among the components used in gasoline blending, certain isoparaffins are ideal for producing clean gasoline due to their high octane rating and low density. The requirements for the hydrocarbon composition of naphtha vary depending on its various uses, and there is a certain degree of complementarity among these needs. Therefore, how to make efficient use of the limited resources of naphtha in order to maximize its benefits in production, ensuring that it is used for aromatic compounds where appropriate and for olefins where suitable, has become an important challenge for integrated oil refining and chemical manufacturing companies. In the past, the conventional practice in refining companies was to separate naphtha into light and heavy fractions, using the light naphtha as a raw material for ethylene production or as a component in gasoline formulations, while the heavy naphtha was used as a feedstock for reforming. This approach failed to enable optimal utilization of naphtha in terms of its hydrocarbon composition. In recent years, the rapid development of naphtha separation technology has made it possible to achieve an optimized utilization of naphtha in terms of its hydrocarbon composition. Representative normal alkane separation technologies include UOP’s MaxEne and Isosiv processes in the United States, as well as Sinopec’s fixed-bed twin-tower parallel naphtha adsorption separation process. UOP’s MaxEne process uses mixed straight-run naphtha as raw material, and employs UOP’s MaxEne simulated moving bed adsorption separation technology to separate the n-paraffins from the isoparaffins in the mixed straight-run naphtha. Normal alkanes are first selectively adsorbed from naphtha, and then desorbed using an alkane-based desorbent; the desorbent is recovered by distillation and reused. This process produces two streams of products; the \"extract\" is a concentrated mixture of n-alkanes, which is fed into a naphtha cracking unit, enabling an increase in the yield of ethylene by over 30%, while the yield of propylene remains essentially unchanged ; “The residue consists of aromatic hydrocarbons, naphthenes, and isoparaffins; its octane rating increases by more than 6%, allowing it to be used directly in gasoline blending or further processed in a reforming unit. In 2013, Sinopec put into operation the MaxEne unit that utilizes UOP technology. Since its commissioning, this unit has processed over 3 million tons of naphtha in total, and all production parameters, including quality and quantity, meet the specified standards, thereby significantly increasing the overall yield of downstream petrochemical products. The adsorbent used in the MaxEne process is ADS-410 developed by UOP, while the desorbent is n-dodecane; currently, the desorbent is available in bulk supply from domestic companies. According to production data, by adopting the MaxEne process, existing naphtha cracking units can increase ethylene yield by up to 40% without affecting propylene production. At the same time, the production of reformed oil, which is used as a component in gasoline blending, can be increased by 5%, while the production of aromatics can be raised by around 10%.
Reply #22017-03-01
Could the poster send me some detailed information? Thank you! 1733275625@qq.com
Reply #32017-03-01
After checking, the desorbent is the key issue. At present, the quality parameters of n-dodecane obtained through the separation and purification of the NC10-C13 mixture produced by Jinling Petrochemical’s alkylbenzene plant meet UOP’s requirements. Is this desorbent related to extraction reactions, utilizing the difference in solubility between two components to separate the raffinate from the extract? This project is quite good; I hope that companies in China can develop such advanced technology.
Reply #42017-03-11
This post was last edited by peterjfpan on 2017-3-11 22:04: “Ethylene yield increased by up to 40%. At the same time, the production of reformed oil, which is used as a component in gasoline blending, can be increased by 5%, while the production of aromatics can be raised by around 10%. ” Are these data the actual operational figures for Yangzi Petrochemical, or are they estimated values? If so, could you explain the estimation method? Firstly, logically speaking, MaxEne enables the separation of normal and isomeric compounds in the naphtha fraction; it only carries out the separation process and does not produce a final product. Therefore, it is impossible to measure the benefits, as these can only be determined through the performance of the ethylene plant and the reforming unit. Hence, the data mentioned above is very important ; We are all aware of normal olefins and isomerized olefins, but we still lack data to determine the extent of their impact on ethylene and reforming. For ethylene, there are yield models available for calculation (I can’t remember the name Spyroo???); reformation can also be calculated using reformation yield models. So it is expected that such calculations are possible, but actual operational data would be even better. After all, the MaxEne process does not generate benefits directly; rather, it consumes a certain amount of energy. It depends on whether the benefits it can bring downstream are substantial. . . . If the benefits are proven, then the integration of large-scale refining and ethylene chemical industries would be an excellent option to consider. MaxEne is merely one application of the Molex process, used for the separation of ortho and para isomers in naphtha fractions. It has also been mentioned that the 1,2-dodecene separation processes in Jinling and Fushun represent other applications of the Molex process; Molex involves adsorption separation, utilizing shape-selective molecular sieves to separate ortho and para isomers. Different applications simply use different molecular sieves.
Reply #52017-03-11
This post was last edited by peterjfpan on 2017-3-11 at 22:19. The understanding that \"this desorbent is involved in a type of extraction reaction, using the different solubilities of the two components to separate the raffinate from the extract\" is incorrect; what is discussed here is adsorption separation, not absorption-desorption or dissolution/extraction separation. The adsorbent is a solid, and when the mixed feedstock passes through this solid adsorbent, separation takes place due to the different adsorption coefficients of various components. The components that are adsorbed onto the solid are then displaced from there using another component, namely the desorbent. This process makes use of simulated moving bed technology. Are you familiar with chromatography columns? It’s based on the same principle.
Reply #62017-03-11
Thank you for the guidance. I see now; it’s the adsorption principle, not the extraction principle
Reply #72017-03-13
In the context of adsorption and analysis mentioned here, is a liquid phase being used?

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