NOVELTY - The system comprises a first feedstock that comprises hydrocarbons and is fed to a steam reformer (220) to produce synthesis gas (228) comprising carbon monoxide and excess hydrogen, a methanol reactor to produce methanol from the synthesis gas, an oil hydroprocessing reactor (250) to receive the excess hydrogen, and a second feedstock comprising an oil that is fed to the hydroprocessing reactor and mixed with the excess hydrogen for hydroprocessing reactions to produce a hydrocarbon product from the oil. The excess hydrogen is separated from methanol produced by the methanol reactor.    USE - The system is useful for integrating methanol production and hydroprocessing of oil feedstock for producing a 50% renewable methanol product such as renewable liquefied petroleum gas product, a renewable naphtha product, a renewable diesel product or a renewable gasoline product (all claimed).    ADVANTAGE - The system is capable of efficiently integrating methanol production and hydroprocessing of oil feedstock thus economically producing the methanol product with high quality and reducing the levels of carbon emissions, consumption of non-renewable resources and environmental impact during the generation of the methanol product.    DETAILED DESCRIPTION - The system comprises a first feedstock that comprises hydrocarbons and is fed to a steam reformer (220) to produce synthesis gas (228) comprising carbon monoxide and excess hydrogen, a methanol reactor to produce methanol from the synthesis gas, an oil hydroprocessing reactor (250) to receive the excess hydrogen, and a second feedstock comprising an oil that is fed to the hydroprocessing reactor and mixed with the excess hydrogen for hydroprocessing reactions to produce a hydrocarbon product from the oil. The excess hydrogen is separated from methanol produced by the methanol reactor, and is supplied directly from the steam reformer to the oil hydroprocessing reactor. The hydrocarbons of 1-4C and 1-2C are separated from the hydrocarbon product and recycled to the first feedstock. The hydrocarbons of 3-4C are separated from the hydrocarbon product as LPG fuel. The hydrocarbons of 5-16C are separated from the hydrocarbon product as fuels. The hydrocarbons of 17C or greater are separated from the hydrocarbon product and recycled to the second feedstock. The fuels comprise naphtha and diesel, and are processed to produce upgraded fuels. The naphtha is upgraded in a catalytic reformer step to a gasoline. The diesel is upgraded in a hydroisomerization step to a jet fuel. The second feedstock comprises bio-oil (1-100 %), crude oil (0-99%), coal oil (0-99%), paraffinic gas condensate (0-99%), and detergent. The hydroprocessing reactions are catalytic hydroprocessing reactions utilizing a catalyst comprising active metals. The catalyst comprises group VIB metal and/or metal group VIII metal, and is a cobalt-molybdenum, nickel-molybdenum or nickel-tungsten type catalyst. The hydroprocessing reactor is a single stage hydroprocessing reactor, a multi-bed hydroprocessing reactor, a series flow hydroprocessing reactor and two stage hydroprocessing reactor. INDEPENDENT CLAIMS are included for:    (1) a process for integrating a methanol plant with an oil hydroprocessing plant;    (2) a process for producing a fuel product; and    (3) an integrated methanol processing and oil hydroprocessing plant.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a methanol plant integrated with an oil hydroprocessing plant.    Methanol processing plant (230)    Hydrocarbon feedstock (212)    Steam reformer (220)    Synthesis gas (228)    Synthesis reactor (230)    Hydroprocessing reactor. (250)