A system is provided integrating a steam pyrolysis zone integrated with a solvent deasphalting zone to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromatics.

A system is provided integrating a steam pyrolysis zone integrated with a solvent deasphalting zone to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromatics.

A process and apparatus for oxidizing thiol compounds from an alkaline stream. The process includes passing a thiol rich alkaline stream and an oxygen containing gas to a low pressure oxidizing zone to oxidize at least a portion of the thiol compounds to disulfide compounds. A liquid stream comprising the alkali containing the disulfide compounds is passed through a pump to increase the pressure and form a pressurized alkaline stream. The pressurized alkaline stream and a sulfur lean liquid light hydrocarbon stream are introduced to a high pressure disulfide separation vessel to form a sulfur lean alkaline stream and a sulfur rich liquid light hydrocarbon stream.

At least one pH-sensitive component may contact a refinery stream for measuring the pH of the refinery stream. A light from a light source may be emitted onto the pH-sensitive component, and a detector may detect a first luminescence or color change of chromophore measurement radiated from the pH-sensitive component. A first pH of the refinery stream may be determined from the first luminescence or color change of chromophore measurement.

At least one pH-sensitive component may contact a refinery stream for measuring the pH of the refinery stream. A light from a light source may be emitted onto the pH-sensitive component, and a detector may detect a first luminescence or color change of chromophore measurement radiated from the pH-sensitive component. A first pH of the refinery stream may be determined from the first luminescence or color change of chromophore measurement.

A process for taking non-treated re-refined vacuum gas oil and pretreating the product before the product is hydrotreated and used for fuel oil blends.

A process for taking non-treated re-refined vacuum gas oil and pretreating the product before the product is hydrotreated and used for fuel oil blends.

One exemplary embodiment can be a process for removing gases from a sweetened hydrocarbon stream. The process can include passing the sweetened hydrocarbon stream to a gas removal zone, contacting the sweetened hydrocarbon stream with an aqueous stream, passing the aqueous stream to the degassing drum, and removing gases including at least one of oxygen and nitrogen from the aqueous stream. Often, the gas removal zone includes a degassing drum.

One exemplary embodiment can be a process for removing gases from a sweetened hydrocarbon stream. The process can include passing the sweetened hydrocarbon stream to a gas removal zone, contacting the sweetened hydrocarbon stream with an aqueous stream, passing the aqueous stream to the degassing drum, and removing gases including at least one of oxygen and nitrogen from the aqueous stream. Often, the gas removal zone includes a degassing drum.

The present technology provides a process that includes heating a first mixture of elemental sulfur and particles comprising an alkali metal sulfide in a liquid hydrocarbon to a temperature of at least 150 C., to provide a sulfur-treated mixture comprising agglomerated particles; and separating the agglomerated particles from the sulfur-treated mixture to provide a desulfurized liquid hydrocarbon and separated solids. This process may be used as part of a suite of processes for desulfurizing liquid hydrocarbons contaminated with organosulfur compounds and other heteroatom-based contaminants. The present technology further provides processes for converting carbon-rich solids (e.g., petroleum coke) into fuels.