HCBBS Forum (English)
Submit Chemical Projects / Find Solutions
Amplify Your Requirements on a Broader Chemical Platform *Engineering · Technology · Equipment · Solutions*
Submit Request

Advanced desulfurization technology for cracked diesel

2009-03-01View Original

Thread Content

Desulfurization of cracked diesel is one of the methods to alleviate oil shortages. However, advanced technology is required to achieve diesel of high quality. Of course, cracking technology may be unfair to coal resources, and it often gives the impression of being somewhat exploitative. Therefore, if it is to be carried out, it should be done as well as possible. I look forward to your insights.
Reply #22009-03-01
Please refer to the following link; it may be helpful to you: http://bbs.hcbbs.com/viewthread.php?tid=96920&highlight=%B2%F1%D3%CD%2B%CD%D1%C1%F2
Reply #32009-03-01
Adopting a new mild hydrocracking route enables the conversion of vacuum gas oil (VGO) to increase diesel production. Meanwhile, the hydrocracking reaction improves the quality of the remaining VGO, making it an excellent feedstock for catalytic cracking (FCC), and it also increases gasoline yield and facilitates the production of low-sulfur diesel. Typically, to produce diesel with 10 μg/g of sulfur via hydrocracking, it is necessary to carry out the process under medium to high pressure (greater than 12 MPa), resulting in a relatively high conversion rate (greater than 50%). When mild hydrocracking (MHC) is used, although the pressure is low to medium (5 – 12 MPa) and the conversion rate ranges from 20% to 40%, it is difficult for the diesel fraction obtained through MHC to meet the requirement of a sulfur content of 10 μg/g. Additionally, when hydrogenated VGO is used as feed for FCC, the sulfur content in the diesel increases both at the beginning and at the end of operation. To address both of these issues simultaneously, Europe has developed a new patented process that allows for independent control of diesel quality. The new process takes MHC as the core and combines specialized purification stages to form an integrated process. Fresh VGO feed is mixed with recycled hydrogen and fed into the MHC reactor, while the hydrogenated VGO fraction is sent to the FCC unit. The diesel fraction is then mixed with fresh hydrogen and fed into a dedicated single-pass refining reactor. The refining reactor uses a high hydrogen partial pressure to ensure maximum hydrorefining of diesel that is difficult to desulfurize by hydrogenation. Compared to two separate units, this process saves on equipment investment and operating costs, reduces the need for compressors and air coolers, and enables flexible heat integration. It allows diesel from units such as distillation, FCC, viscosity reduction, and coking to also be fed into the refining reactor for refinement. A new unit using this process was put into operation in the second half of 2004 at the Puertillano refinery of Repsol-YPF in Spain, with an MHC conversion rate of 35%, enabling the production of diesel containing 10 μg/g of sulfur. By using SR (straight-run) VGO and coker heavy gas oil (high in nitrogen), diesel with 33.6% (by volume) sulfur content can be produced

Submit a Project

**Looking for Chemical Technology, Equipment & Solutions?** No Registration Required Broader Platform Exposure | Global Chemical Service Provider Connections

Submit Request — Free Consultation

Disclaimer

This is an automated machine translation of the original thread. Some technical terms may have inaccuracies; the original text shall prevail. Click "View Original" at the top right to access the source page, which supports IP-based automatic real-time language translation. Please watch out for contact details and sales inducements to prevent fraud. All content and translations are for reference only, representing solely the poster's personal views. For enquiries, email service@hcbbs.com.