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Distillation

Editorial Comment: HPI spending in 2019 forecast at $375 B

Hydrocarbon Processing Staff: Nichols, Lee

Regulations, feedstock advantages, supply/demand gaps, etc., are resulting in a surge of new capital investments around the world.

Process design consideration for a deep-cut vacuum distillation unit—Part 2

Recently, many US refineries have been reconfigured to process heavy opportunistic sour crudes.

Conceptualizing a mega-integrated refinery and petrochemical complex: A case study

Fluor Daniel India Pvt. Ltd.: Chaudhuri, S.  |  Dass, T.

<i>Integration</i> is the new keyword for sustainability and profit in today’s oil and gas market scenario.

Process design consideration for a deep-cut vacuum distillation unit—Part 1

In the recent past, many US refineries have been reconfigured to process heavy opportunistic sour crudes.

Reconstruct a vacuum column injector system using computer modeling—Part 1

Kazan National Research Technological University: Telyakov, E. S.  |  Osipov, E. V.  |  Bugembe, D.

Steam ejector vacuum systems are the most common means of creating and maintaining a vacuum in the process units of oil and gas processing facilities.

Industry Perspectives: Refining’s real growth is through secondary unit capacity

Hydrocarbon Processing Staff: Nichols, Lee

According to multiple industry reports, the global refining sector will add between 7 MMbpd and 8 MMbpd of new crude distillation unit (CDU) capacity by the early 2020s.

Global Project Data

Hydrocarbon Processing Staff: Nichols, Lee

According to <i>Hydrocarbon Processing</i>’s Construction Boxscore Database, there are nearly 470 active refining projects around the globe.

Hydrocarbon Processing Awards

<i>Hydrocarbon Processing,</i> the downstream processing sector’s leading technical publication, has announced the winners for its second annual awards.

Additive solutions to SOx emissions in FCCUs

Tüpraş: Genç, M.  |  Dalgıç, E.  |  Karani, U.  |  Emiroglu, I.  |  Er, I.  |  Gül, A.  |  Avcilar, S.
Johnson Matthey Process Technologies: Ventham, T.

Sulfur oxide additives are typically based on hydrotalcite or magnesium aluminate spinel-type structures. Magnesium alumina is the pickup agent present in the most effective SO<sub>x</sub> additives on the market; therefore, to optimize SO<sub>x</sub> reduction, it is critical to maximize the amount of the critical magnesium component in the fluid catalytic cracking unit (FCCU) in an efficient and cost-effective way.

Business Trends: A strategic energy solution

Foster Wheeler: Giglio, R.

Refining is the process of separating crude oil into different hydrocarbon groups through distillation.