Process for transportation and distillation of petroleum with methanol

Claim 2

In a process for the production of petroleum products which includes the steps of recovering crude petroleum from an oil well, transporting recovered crude petroleum to a refinery location remote from the oil well, refining crude petroleum at the refinery location, and recovering a petroleum distillate fraction having utility as a motor fuel, and wherein a difficult to transport fossil fuel selected from natural gas, coal and a difficult to transport crude petroleum is available in the vicinity of the oil well, the improvement comprising converting said difficult to transport fossil fuel to methanol, admixing the resulting methanol with recovered crude petroleum in an amount to form a stable, pumpable emulsion consisting essentially of only methanol and crude petroleum, transporting the recovered crude petroleum to the remote refinery location in the form of said stable, pumpable, methanol-crude petroleum emulsion, breaking the emulsion at the refinery location by distillation, and recoverying from the distillation step a methanol-hydrocarbon azeotrope fraction having utility as a motor fuel, having a boiling point of about 63° C., and containing in addition to methanol at least 50% by weight of hydrocarbons boiling in the range of from about 70° C. to about 120° C.

Claim 3

A process according to claim 1 wherein, said step of forming the stable pumpable methanol-crude petroleum emulsion comprises, admixing about 20% by weight of methanol based on the total weight of hydrocarbons boiling in the temperature range of from about 70° C. to about 120° C. at atmospheric pressure, so that the recovered hydrocarbon azeotrope fraction having a boiling of about 63° C. contains about 20% methanol.

Claim 4

In a process for the production of petroleum products which includes the steps of recovering crude petroleum from an oil well, transporting recovered crude petroleum to a refinery location remote from the oil well, refining crude petroleum at the refinery location, and recovering a petroleum distillate fraction comprising hydrocarbons boiling in the range of from about 70° C. to about 120° C. and having utility as a motor fuel, and wherein a fossil fuel selected from coal, natural gas and crude petroleum is available in the vicinity of the oil well, the improvement comprising converting said fossil fuel to methanol, admixing the resulting methanol with crude petroleum to form a stable, pumpable methanol-crude petroleum emulsion, transporting the recovered crude petroleum to the refinery location in the form of said stable methanol-crude petroleum emulsion, breaking the emulsion at the refinery location by distillation in a distillation zone, recovering from the distillation zone a methanol-hydrocarbon azeotrope fraction comprising methanol and hydrocarbons which boil in the range of from about 70° C. to about 120° C., said azeotrope fraction having a boiling point of about 63° C. and having utility as a motor fuel, and controlling the amount of the methanol in the methanol-crude petroleum emulstion introduced into the distillation zone so as to correspond approximately to the proportion of hydrocarbons present in the crude petroleum that boil in the range of from about 70° C. to about 120° C., whereby essentially all the hydrocarbons present in the crude petroleum that boil in the range of from about 70° C. to about 120° C. appear in said methanol-hydrocarbon azeotrope fraction.

Claim 5

In a process for the production of petroleum products which includes the steps of recovering crude petroleum from an oil well, transporting recovered crude petroleum to a refinery location remote from the oil well, refining crude petroleum at the refinery location, and recovering a petroleum distillate fraction comprising hydrocarbons boiling in the range of from about 70° C. to about 120° C. and having utility as a motor fuel, and wherein a fossil fuel selected from coal, natural gas and crude petroleum is available in the vicinity of the oil well, the improvement comprising converting said fossil fuel to methanol, admixing the resulting methanol with crude petroleum to form a stable, pumpable methanol-crude petroleum emulsion, transporting the recovered crude petroleum to the refinery location in the form of said stable methanol-crude petroleum emulsion, breaking the emulsion at the refinery location by distillation in a distillation zone, recovering from the distillation zone a methanol-hydrocarbon azeotrope fraction comprising methanol and hydrocarbons which boil in the range of from about 70° C. to about 120° C., said azeotrope fraction having a boiling point of about 63° C. and having utility as a motor fuel, and controlling the amount of the methanol in the methanol-crude petroleum emulstion introduced into the distillation zone so as to correspond approximately to the proportion of hydrocarbons present in the crude petroleum that boil in the range of from about 70° C. to about 120° C., whereby essentially all the hydrocarbons present in the crude petroleum that boil in the range of from about 70° C. to about 120° C. appear in said methanol-hydrocarbon azeotrope fraction.

Claim 6

A process according to claim 3, in which distillation is effected by supplying heat at a substantially constant rate.

Claim 7

A process according to claim 3, in which heat is supplied to the distillation vessel at a substantially constant rate during collection of the methanol-containing distillate fraction.

Claim 8

A process according to claim 3, in which the proportion of methanol is so chosen that distillation is carried out in the presence of about 20 weight % of methanol based upon the total weight of hydrocarbons boiling in the temperature range of from about 70° C. to about 120° C. at atmospheric pressure.