An integrated process for producing petrochemicals and fuel products from a crude oil feed comprising: separating from the crude oil feed, in an atmospheric distillation unit, at least a first ADU fraction comprising straight run naphtha, a second ADU fraction comprising at least a portion of middle distillates from the crude oil feed, and a third ADU fraction comprising atmospheric residue; separating from the third ADU fraction, in a vacuum distillation unit, at least a first VDU fraction comprising vacuum gas oil, and a second VDU fraction comprising vacuum residue; hydroprocessing in a distillate hydroprocessing zone middle distillates from the second ADU fraction, and recovering at least a first DHP fraction and a second DHP fraction, wherein the first DHP fraction comprises naphtha and the second DHP fraction is used for diesel fuel production; steam cracking, in a mixed feed steam cracking (MFSC) zone, naphtha from the first ADU fraction and raffinate derived from an aromatics extraction zone, wherein steam cracking in the MFSC zone is under conditions effective to recover a mixed product stream comprising H2, methane, ethane, ethylene, mixed C3s and mixed C4s; pyrolysis gasoline; and pyrolysis oil; recovering, from the mixed product stream, H2, methane, non-olefinic C2-C4s, and petrochemicals ethylene, propylene and butylenes, hydroprocessing pyrolysis gasoline from steam cracking in a naphtha hydroprocessing zone, and recovering hydrotreated pyrolysis gasoline; separating aromatics from hydrotreated pyrolysis gasoline in an aromatics extraction zone for recovery of petrochemical aromatic products, and aromatics extraction zone raffinate, wherein the raffinate derived from aromatics extraction is all or a portion of the aromatics extraction zone raffinate; and hydrocracking at least a portion of the vacuum residue in a vacuum residue hydrocracking zone (VRHCK), recovering VRHCK products boiling at or below an atmospheric residue end boiling point and including LPG naphtha and middle distillate range components, and recovering VRHCK hydrocracked gas oil. separating from the crude oil feed, in an atmospheric distillation unit, at least a first ADU fraction comprising straight run naphtha, a second ADU fraction comprising at least a portion of middle distillates from the crude oil feed, and a third ADU fraction comprising atmospheric residue; a first ADU fraction comprising straight run naphtha, a second ADU fraction comprising at least a portion of middle distillates from the crude oil feed, and a third ADU fraction comprising atmospheric residue; separating from the third ADU fraction, in a vacuum distillation unit, at least a first VDU fraction comprising vacuum gas oil, and a second VDU fraction comprising vacuum residue; a first VDU fraction comprising vacuum gas oil, and a second VDU fraction comprising vacuum residue; hydroprocessing in a distillate hydroprocessing zone middle distillates from the second ADU fraction, and recovering at least a first DHP fraction and a second DHP fraction, wherein the first DHP fraction comprises naphtha and the second DHP fraction is used for diesel fuel production; steam cracking, in a mixed feed steam cracking (MFSC) zone, naphtha from the first ADU fraction and raffinate derived from an aromatics extraction zone, wherein steam cracking in the MFSC zone is under conditions effective to recover a mixed product stream comprising H2, methane, ethane, ethylene, mixed C3s and mixed C4s; pyrolysis gasoline; and pyrolysis oil; recovering, from the mixed product stream, H2, methane, non-olefinic C2-C4s, and petrochemicals ethylene, propylene and butylenes, hydroprocessing pyrolysis gasoline from steam cracking in a naphtha hydroprocessing zone, and recovering hydrotreated pyrolysis gasoline; separating aromatics from hydrotreated pyrolysis gasoline in an aromatics extraction zone for recovery of petrochemical aromatic products, and aromatics extraction zone raffinate, wherein the raffinate derived from aromatics extraction is all or a portion of the aromatics extraction zone raffinate; and hydrocracking at least a portion of the vacuum residue in a vacuum residue hydrocracking zone (VRHCK), recovering VRHCK products boiling at or below an atmospheric residue end boiling point and including LPG naphtha and middle distillate range components, and recovering VRHCK hydrocracked gas oil.