High catalyst selectivity prompts cycle length extension at Petro Rabigh monoethylene glycol plant
Published by Nicholas Woodroof,
Editor
Hydrocarbon Engineering,
The plant uses the Shell OMEGA process, which is based on the catalytic conversion of both ethylene to ethylene oxide and ethylene oxide to ethylene glycol.
Ethylene oxide catalyst selectivity is a key factor in the efficiency of MEG production: a higher selectivity means that smaller volumes of raw material are required to manufacture the product. The cycle that started in May 2020 marked a change in catalyst from Shell Catalysts & Technologies’ S-888 (which had achieved an initial selectivity of 90.9%) to S-889 catalyst. The resulting improvement of just over 1% will deliver significant savings and lead to higher profitability or enhanced competitiveness in what is, at present, a very challenging market. This catalyst upgrade is expected to reduce raw materials requirements by 4000 tpy for ethylene and 14 000 tpy for oxygen. Over a full cycle, these reductions could translate into a multimillion-dollar saving.
This performance is the result of both the improved catalyst and the way the unit is operated. The Petro Rabigh plant carried out a well-structured catalyst selection process with an emphasis on maximising performance and extending the run length.
The plant has been using Shell Catalysts & Technologies catalysts since 2009. “We have achieved strong results across three- and four-year cycles with earlier-generation catalysts,” explained Saeed Al Ghamdi, Head of Process Engineering at Petro Rabigh. “The stability of the new catalyst, coupled with its increased selectivity, has encouraged us to look at pushing the cycle length to five years.”
Ammar Bakheet, Process Engineer, Petro Rabigh, said: “The results show that, with careful planning and well-managed start-ups and processes, engineers can achieve substantial improvements in performance by moving to the latest generation of catalyst products.”
“The continuous engagement and collaboration with Petro Rabigh were key enablers for selecting the optimum catalyst for Petro Rabigh,” observed Jaafar El-Masri, Technical Service Manager, Shell Catalysts & Technologies. “This will add substantial value in the form of raw materials savings, and I am excited at the prospect of seeing the current catalyst batch run for the full five years.”
Read the article online at: https://www.hydrocarbonengineering.com/petrochemicals/17022021/high-catalyst-selectivity-prompts-cycle-length-extension-at-petro-rabigh-monoethylene-glycol-plant/
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