Refininghttp://www.hydrocarbonprocessing.com/RSS.aspx?FeedID=1806&copy;2016 Hydrocarbon Processing60RefiningAn operations reference model for common refinery operationshttp://www.hydrocarbonprocessing.com/Article/3566701/An-operations-reference-model-for-common-refinery-operations.htmlFri, 01 Jul 2016 00:00:00 GMTAsia’s smaller downstream players have big planshttp://www.hydrocarbonprocessing.com/Article/3566294/Asias-smaller-downstream-players-have-big-plans.htmlFri, 01 Jul 2016 00:00:00 GMTCatalytic advances make chemical upgrading a reality for heavy sour feedshttp://www.hydrocarbonprocessing.com/Article/3566696/Catalytic-advances-make-chemical-upgrading-a-reality-for-heavy-sour-feeds.htmlFri, 01 Jul 2016 00:00:00 GMTEnvisioning a “future-proof” refinery of the futurehttp://www.hydrocarbonprocessing.com/Article/3566677/Envisioning-a-future-proof-refinery-of-the-future.htmlFri, 01 Jul 2016 00:00:00 GMTExperimental study of flow-induced pipe vibrations with guided end conditionshttp://www.hydrocarbonprocessing.com/Article/3567083/Experimental-study-of-flow-induced-pipe-vibrations-with-guided-end-conditions.htmlFri, 01 Jul 2016 00:00:00 GMTExplore alternative engineering options for code requirementshttp://www.hydrocarbonprocessing.com/Article/3566671/Explore-alternative-engineering-options-for-code-requirements.htmlFri, 01 Jul 2016 00:00:00 GMTHP Industry Metricshttp://www.hydrocarbonprocessing.com/Article/3566305/HP-Industry-Metrics.htmlFri, 01 Jul 2016 00:00:00 GMTHP Peoplehttp://www.hydrocarbonprocessing.com/Article/3566683/HP-People.htmlFri, 01 Jul 2016 00:00:00 GMTMinimize industrial cyber security risk in plants in 12 stepshttp://www.hydrocarbonprocessing.com/Article/3566721/Minimize-industrial-cyber-security-risk-in-plants-in-12-steps.htmlFri, 01 Jul 2016 00:00:00 GMTNon-phosphorus corrosion inhibitor optimizes cooling tower uptime for environmental compliance http://www.hydrocarbonprocessing.com/Article/3567142/Non-phosphorus-corrosion-inhibitor-optimizes-cooling-tower-uptime-for-environmental-compliance.htmlFri, 01 Jul 2016 00:00:00 GMTSecure the best benefit from C<sub>4</sub> hydrocarbon processing—Part 2: Economic evaluationhttp://www.hydrocarbonprocessing.com/Article/3566725/Secure-the-best-benefit-from-C4-hydrocarbon-processingPart-2-Economic-evaluation.htmlFri, 01 Jul 2016 00:00:00 GMTTackle operational challenges in refining unconventional crudeshttp://www.hydrocarbonprocessing.com/Article/3566664/Tackle-operational-challenges-in-refining-unconventional-crudes.htmlFri, 01 Jul 2016 00:00:00 GMTTeaching an old plant new tricks: The rise of the methanol plant revamphttp://www.hydrocarbonprocessing.com/Article/3566708/Teaching-an-old-plant-new-tricks-The-rise-of-the-methanol-plant-revamp.htmlFri, 01 Jul 2016 00:00:00 GMTRefinery investments focus on ultra-low-sulfur gasolinehttp://www.hydrocarbonprocessing.com/Article/3558206/Refinery-investments-focus-on-ultra-low-sulfur-gasoline.htmlMon, 06 Jun 2016 00:00:00 GMT“Intelligizing” the refinery for business sustainabilityhttp://www.hydrocarbonprocessing.com/Article/3558221/Intelligizing-the-refinery-for-business-sustainability.htmlWed, 01 Jun 2016 00:00:00 GMTA new solution to the challenges of crude selection and schedulingThe state-of-the-art approach to solving the crude selection and scheduling (CSS) problem is to separate the two challenges. Linear programs (LPs) are used for crude selection to calculate the optimal crude schedule for a given time frame, generally a month. The pipeline pumping schedule from a crude terminal to the refinery is generated by a simulation scheduling calculation.http://www.hydrocarbonprocessing.com/Article/3558696/A-new-solution-to-the-challenges-of-crude-selection-and-scheduling.htmlWed, 01 Jun 2016 00:00:00 GMTCatalyst replacement strategy for a hydrocracking unit at a Middle East refineryhttp://www.hydrocarbonprocessing.com/Article/3558623/Catalyst-replacement-strategy-for-a-hydrocracking-unit-at-a-Middle-East-refinery.htmlWed, 01 Jun 2016 00:00:00 GMTHP Industry Metricshttp://www.hydrocarbonprocessing.com/Article/3558195/HP-Industry-Metrics.htmlWed, 01 Jun 2016 00:00:00 GMTHP Innovationshttp://www.hydrocarbonprocessing.com/Article/3558225/HP-Innovations.htmlWed, 01 Jun 2016 00:00:00 GMTHP Peoplehttp://www.hydrocarbonprocessing.com/Article/3558710/HP-People.htmlWed, 01 Jun 2016 00:00:00 GMTImprove refinery compressor performance with a reengineered rotorhttp://www.hydrocarbonprocessing.com/Article/3558687/Improve-refinery-compressor-performance-with-a-reengineered-rotor.htmlWed, 01 Jun 2016 00:00:00 GMTMeeting Africa’s demand for oil productshttp://www.hydrocarbonprocessing.com/Article/3558210/Meeting-Africas-demand-for-oil-products.htmlWed, 01 Jun 2016 00:00:00 GMTOptimize isomerization reactor temperatures and component RONhttp://www.hydrocarbonprocessing.com/Article/3558558/Optimize-isomerization-reactor-temperatures-and-component-RON.htmlWed, 01 Jun 2016 00:00:00 GMTOvercome biases and challenges facing industryhttp://www.hydrocarbonprocessing.com/Article/3558200/Overcome-biases-and-challenges-facing-industry.htmlWed, 01 Jun 2016 00:00:00 GMTPyrometer temperature measurement corrections ensure reliable reformer operationhttp://www.hydrocarbonprocessing.com/Article/3558702/Pyrometer-temperature-measurement-corrections-ensure-reliable-reformer-operation.htmlWed, 01 Jun 2016 00:00:00 GMTReduce revamp costs with appropriate 3D laser scanning strategieshttp://www.hydrocarbonprocessing.com/Article/3558704/Reduce-revamp-costs-with-appropriate-3D-laser-scanning-strategies.htmlWed, 01 Jun 2016 00:00:00 GMTSecure the best benefits from C<sub>4</sub> hydrocarbon processing—Part 1: Separation sequenceshttp://www.hydrocarbonprocessing.com/Article/3558709/Secure-the-best-benefits-from-C4-hydrocarbon-processingPart-1-Separation-sequences.htmlWed, 01 Jun 2016 00:00:00 GMTSyngas from H<sub>2</sub>S and CO<sub>2</sub>: An alternative, pioneering synthesis route?Hydrogen sulfide (H<sub>2</sub>S) and carbon dioxide (CO<sub>2</sub>) represent major concerns for the hydrocarbon industry. Both species are contaminants and, since their use as feedstock is minor, are considered troubling byproducts. H<sub>2</sub>S, which mainly derives from oil and gas desulfurization, cannot be vented. Consequently, neutralization is mandatory. Practically every refinery is equipped with a Claus sulfur recovery unit (SRU). Flue gases rich in CO<sub>2</sub> are vented, contributing to climate change; sequestration of CO<sub>2</sub> is technically viable, but remote disposal still remains a questionable end.http://www.hydrocarbonprocessing.com/Article/3558601/Syngas-from-H2S-and-CO2-An-alternative-pioneering-synthesis-route.htmlWed, 01 Jun 2016 00:00:00 GMTWill India be Asia’s next downstream powerhouse?http://www.hydrocarbonprocessing.com/Article/3558187/Will-India-be-Asias-next-downstream-powerhouse.htmlWed, 01 Jun 2016 00:00:00 GMT