In a method of producing a hydrocarbon-based synthetic fuel by adding water to a base oil, it is intended to increase a ratio of the synthetic fuel to a hydrocarbon-based fuel as the base oil, more significantly than ever before. Specifically, provided is a method of producing a hydrocarbon-based synthetic fuel oil having a volume greater than that of a hydrocarbon-based base fuel oil, by adding water to the hydrocarbon-based base fuel oil, wherein a first-order hydrocarbon-based synthetic fuel oil produced by the production method is used as a base fuel oil for producing a second-order hydrocarbon-based synthetic fuel oil, or this process is repeated plural times in sequence, thereby producing a hydrocarbon-based synthetic fuel having a high water addition rate.

A secondary fluid is provided for use in an internal combustion engine that burns a primary fuel. The secondary fluid comprises about 15 vol % to about 30 vol % of alcohol; and about 0.0025 vol % to about 0.5 vol % of a lubricity enhancer which optionally is a castor oil. The secondary fluid is a thermodynamically stable microemulsion with water being the continuous phase.

Processes for stabilizing toluenediamine residues are disclosed. These processes include adding a low viscosity, low boiling liquid to a toluenediamine residue composition to form a blend, and optionally, continuously monitoring the viscosity of the blend during addition of the low viscosity, low boiling liquid. The low viscosity, low boiling liquid may be added at 5% to 30% by weight based on the total weight of the blend. Further, the low viscosity, low boiling liquid may be added so that the blend has a viscosity of 10,000 cP or less throughout the temperature range of 40 C. to 95 C. Blends of toluenediamine residue compositions and low viscosity, low boiling liquids such as water, and methods of their use as a fuel are also disclosed.

The present disclosure provides compositions and methods of use of cashew nut shell liquid (CNSL) and its derivatives as one of the components for decreasing the viscosity of heavy oils, extra heavy oils, high asphaltene natural bitumen, and tar sands (i.e., heavy oils). The decrease in viscosity of heavy oils increases the ability of the heavy oil mixture to be piped, transported, stored and used. The present disclosure provides compositions containing at least one of anacardic acid, cardanol and cardol, and at least one of a surfactant, a co-solvent, and water. The present disclosure provides compositions that are useful as viscosity reducing agents, heavy oil upgrading agents, wellbore cleaning agents, enhanced oil recovery agents, and cleaning agents for asphaltene-containing materials. Biofuel compositions are also provided by the present disclosure.

There is provided a process for producing a fuel comprising: sensing the sulphur content of a liquid hydrocarbonaceous material; admixing liquid aqueous material and the liquid hydrocarbonaceous material in a predetermined ratio, based upon the sensed sulphur content, such that a nanoemulsion is obtained; and converting the nanoemulsion into at least the fuel.

The present invention provides a desulfurization agent mixing system for fuel oil used in harbors, the system including: a fuel oil tank for storing fuel oil; a desulfurization agent tank for storing a desulfurization agent; a line mixer receiving and mixing the fuel oil and the desulfurization agent from the fuel oil tank and the desulfurization agent tank; a droplet atomization unit for forming droplets of a mixture of the fuel oil and the desulfurization agent, the mixture being generated by the line mixer; a magnetization unit for magnetizing the mixture in which the droplets are contained; a vortex reaction unit for turning the mixture of the fuel oil and the desulfurization agent, which is magnetized by the magnetization unit; a gas separation unit configured to separate gas contained in the fuel oil and the desulfurization agent mixture in the vortex reaction unit; a collision emulsion unit configured to cause the mixture of the fuel oil and the desulfurization agent from which the gas is separated by the gas separation unit to collide against a collision target; and an emulsion tank for storing the mixture of the fuel oil and the desulfurization agent, which is collided by the collision emulsion unit.

Proposed is a method of emulsifying fuel oil and a desulfurization agent. The method includes (a) a step of adding a desulfurization agent to fuel oil for line mixing thereof, (b) a step of generating droplets in the resulting mixture of step (a), (c) a step of causing the resulting mixture of step (b) to pass through a magnetic field so that the mixture can be magnetized, (d) a step of subjecting the resulting mixture of step (c) to vortex mixing, and (e) a step of causing collision of the resulting mixture of step (d). The method uses fuel oil as a continuous phase and a water-based desulfurization agent as a disperse phase and emulsifies the desulfurization agent in the fuel oil through water-in-oil (W/o) emulsification so that the desulfurization agent can be stably dispersed in the fuel oil. Since the fuel oil and the desulfurization agent are burned together during combustion, sulfur oxides that may occur during the combustion are removed, whereby sulfur oxide emissions are reduced.

An industrial fluid is disclosed. The fluid comprises an oleaginous component, an aqueous component, and a surfactant. Substantially all of the surfactant is bound within micelles of the oleaginous component. This results in there being substantially no unbound surfactant present in the fluid. The industrial fluid is also substantially flee from insoluble defoamers or anti-foam compounds.

An industrial fluid is disclosed. The fluid comprises an oleaginous component, an aqueous component, and a surfactant dispersed in the aqueous component. The average micelle diameter follows a Gaussian distribution having a mean, , and wherein the standard deviation is less than or equal to 0.2. The industrial fluid is also substantially free from defoamers or anti-foam compounds.

An industrial fluid is disclosed. The fluid comprises an oleaginous component, an aqueous component, and a surfactant dispersed in the aqueous component. The industrial fluid does not contain defoamers or anti-foam compounds. The surfactant is bound within micelles of the oleaginous component and the aqueous component.