Petrochemical Design ›› 2025, Vol. 42 ›› Issue (1): 6-8,12.doi: 10.3969/j.issn.1005-8168.2025.01.002
• DESIGN TECHNOLOGY • Previous Articles Next Articles
Zhang Zezhong1, Zhao Chengyang2, Liu Huadong2, Wang Jiakun1
Online:
Published:
Abstract: Ethylene plant, FCC unit and MTO plant produce a considerable amount of C4-C8 olefin fractions as byproducts. Utilizing these low value-added byproducts to produce ethylene/propylene through olefin catalytic cracking can increase the economic benefits of enterprises. The raw material C4-C8 olefin fractions generally contain impurities such as oxides, sulfur and H2O. Not many impurities are produced during catalytic cracking. In order to obtain polymer grade ethylene and propylene products, an adsorption system needs to be set up to remove the impurities entrained into the system by raw material. This article introduces the regeneration process of the adsorption system and the design calculation of related orifices.
Key words: olefin cracking, refining, adsorption, polymer grade ethylene and propylene, dehydration, orifice calculation
Zhang Zezhong, Zhao Chengyang, Liu Huadong, Wang Jiakun. Regeneration of Adsorption System for Olefin Cracking Products and the Design of Orifices[J].Petrochemical Design, 2025, 42(1): 6-8,12.
0 / / Recommend
Add to citation manager EndNote|Reference Manager|ProCite|BibTeX|RefWorks
URL: http://syhgsj.sei.com.cn/EN/10.3969/j.issn.1005-8168.2025.01.002
http://syhgsj.sei.com.cn/EN/Y2025/V42/I1/6
Strategic Analysis of High Quality International Operation of Chinese Refiningand Petrochemical Engineering Companies
Exploration of Project Management in Three ‘New Fields’ of Refining Projects from Perspective of Product Managers
Optimization of Butene Refining Scheme for Polyolefin Plants
Debottlenecking Reconstruction of Butene-1 Refining Unit
Gas Chromatography Configuration in Central Laboratory of Refinery and Petrochemical Complex
Application of High Pressure PSA Technology in Hydrogen Recovery from Methanol Gas
Cited