Marathon Oil Company

James E Tackett, Jr

LaVaun S Merrill, Jr

A system for measuring the physical characteristics of a hydrocarbon places a reference hydrocarbon cell in thermal contact with a sample cell containing an unknown hydrocarbon. A near infrared spectrum measurement is taken of both the cells. Measurement data from the sample cell is adjusted by the measurement data from the reference cell, and the adjusted measurement data is evaluated by a model to predict the characteristics of the sample. The model is built from a teaching set of hydrocarbons having known physical characteristics and the reference hydrocarbon. Each of the teaching set hydrocarbons is measured and then adjusted by a measurement of the same reference hydrocarbon, and the adjusted measurements are used to build the model.

Method for measuring physical properties of hydrocarbons

A conformance improvement treatment process is provided for reducing the permeability of a higher-permeability zone in a subterranean hydrocarbon-bearing formation which is in fluid communication with a lower-permeability zone of the formation. The process includes preparing a gel precursor solution at the surface, injecting the solution into a wellbore penetrating the formation, placing the solution in the higher-permeability zone and gelling the solution therein. In situ gelation of the solution results in substantial permeability reduction to the higher-permeability zone. A specific gel precursor solution is utilized which contains a gelling agent and a polymer formed from at least two distinct monomers wherein the first monomer has a relatively faster, yet controlled, rate of hydrolysis and the second monomer has a relatively slower rate of hydrolysis. Gelation of the solution is delayed until a substantial number of carboxylate groups are formed in situ on the polymer. The gelling agent subsequently reacts with the carboxylate groups to effect gelation of the solution.

Rate controllable gel for conformance improvement treatment in a

Reversible crosslinked polymer gels are prepared by adding a degelling agent precursor to a gelation solution during initial preparation. The precursor is integrated into the resulting gel and undergoes hydrolysis to transform into an active degelling agent which reverses the gel. The process has specific utility to hydrocarbon recovery applications where in situ gels are difficult to contact with conventional reversing agents.

In situ reversible crosslinked polymer gel used in hydrocarbon recovery

The present invention is a process for selectively plugging high permeability zones of a subterranean hydrocarbon-bearing formation by enhancing the delay associated with the in situ formation of a polymer gel. The process comprises predetermining a gelation delay time based on a formation's temperature, permeability and porosity, the distance from the well bore a region to be plugged is located, and a volumetric rate of gelation fluid injection. A gelation solution is then prepared comprising polyacrylamide a polyvalent metal carboxylate crosslinking agent, a gelation delaying agent and a buffer with a pKa of about 3.5 to about 6.8. Gelation delays are achieved by selecting the polyacrylamide concentration, delaying agent concentration and type, and buffer concentration and type, for given formation conditions. Delay times can range from several hours to several weeks at formation temperatures near 176.degree. F. (80.degree. C.) and from several hours to about one day at formation temperatures above about 219.degree. F. (104.degree. C.). The prepared solution is then injected into the formation via a well bore and allowed to gel. The gel selectively plugs high permeability zones within a subterranean hydrocarbon-bearing formation, at temperatures and distances from the well formerly unobtainable, resulting in improved vertical or areal conformance of injected fluids and improved oil production.

Process for enhanced delayed in situ gelation of chromium polyacrylamide

Selective permeability reduction is achieved in a heterogeneous treatment zone of a subterranean hydrocarbon-bearing formation by initially placing a nonselective permeability-reducing material in the high and low permeability regions of the treatment zone. Thereafter, a permeability-restoring agent is placed in the regions behind the permeability-reducing material. The agent contacts all of the material in the low permeability region, reacting with it to restore permeability thereto. However, the agent is consumed by reaction before it contacts all of the material in the high permeability region, thereby leaving a sufficient amount of material in the high permeability region to achieve selective permeability reduction therein.

Selective permeability reduction in a subterranean hydrocarbon-bearing

A beta-alanine-type branched partially hydrolyzed polyacrylamide is added to an aqueous injection fluid to increase the viscosity of the fluid. The polymer resists plugging of the wellbore face and/or matrix pores and is brine tolerant when injected into a subterranean hydrocarbon-bearing formation.

Brine tolerant polymer and oil recovery applications

Brine tolerant polymer for oil recovery applications

The water content of a crude oil containing surfactant is reduced to less than 0.5 weight percent by first conventionally drying the crude oil to a water concentration less than about 10%, then contacting the crude oil with a low molecular weight alcohol to effect a phase separation into an aqueous layer and an oil layer, thereafter separating these layers to obtain a dried oil and an aqueous alcoholic surfactant solution. The alcohol can then be separated from the aqueous alcoholic surfactant solution. The recovered alcohol can be recycled through the system and the recovered surfactant can be reused in another micellar flood.

Process for drying surfactant-containing crude oil

The efficiency of pumping a hydrocarbon slurry in a pipeline is determined prior to transportation by the relationship:

Method for maximizing the pumpability efficiency of a hydrocarbon slurry

The efficiency of a hydrocarbon slurry is maximized by determining the largest percent of economically pumpable distillation overhead that can be obtained from the hydrocarbon. This determination is based on the properties of the overhead as a carrier fluid in the transporting system (e.g. slurry viscosity or pumpability). Once determined, the composition of the optimum overhead is determined by the usual techniques, i.e., by gas chromatographic techniques, to determine its composition and the cut point defined in terms of the composition of the optimum overhead. The composition of the overhead is monitored during the refining process and is compared with the composition of the optimum overhead. The distillation process is then monitored and controlled accordingly to produce an overhead with the desired molecular composition. One advantage of this method is that it limits the amount of undesirable wax crystals in the overhead. The method works particularly well with waxy hydrocarbon mixtures in fractional distillation processes.

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Littleton, CO, United States of America

James E Tackett, Jr