초록 ▼

A process for preparing a bimodal emulsion of viscous hydrocarbon in water includes providing a stream of water at ambient temperature; providing a liquid additive that tends to gel when mixed with water at temperatures less than a gelling temperature TG; heating the stream to provide a heated strea

A process for preparing a bimodal emulsion of viscous hydrocarbon in water includes providing a stream of water at ambient temperature; providing a liquid additive that tends to gel when mixed with water at temperatures less than a gelling temperature TG; heating the stream to provide a heated stream at a temperature TC which is greater than ambient temperature and less than the gelling temperature TG; feeding the heated stream to a mixer having a mixer inlet so as to impart energy to the heated stream; adding the liquid additive to the heated stream downstream of the mixer inlet, whereby the liquid additive mixes with the stream and the energy inhibits gelling of the liquid additive to provide a substantially homogeneous solution of additive in water. The solution is then divided and used to make two different droplet sized emulsions which are mixed to form the bimodal emulsion.

대표청구항 ▼

1. A process for preparing a bimodal emulsion of viscous hydrocarbon in water comprising the steps of:providing a stream of water at ambient temperature; providing at least one liquid additive that tends to gel when mixed with water at temperatures less than a maximum gelling temperature TG of said

1. A process for preparing a bimodal emulsion of viscous hydrocarbon in water comprising the steps of:providing a stream of water at ambient temperature; providing at least one liquid additive that tends to gel when mixed with water at temperatures less than a maximum gelling temperature TG of said liquid additive; heating said stream to provide a heated stream at a temperature TC which is greater than ambient temperature and less than said maximum gelling temperature TG; feeding said heated stream to a static mixer having a mixer inlet so as to impart energy to said heated stream; adding said liquid additive to said static mixer downstream of said mixer inlet, whereby said liquid additive mixes with said stream and said energy is at an effective amount to inhibit gelling of said liquid additive at TC and so as to provide a substantially homogeneous solution of additive in water; dividing said solution into a first portion and a second portion; mixing said first portion with a viscous hydrocarbon in a first dynamic mixer so as to provide a first hydrocarbon in water emulsion having a first average droplet size; mixing said second portion with a viscous hydrocarbon in a second dynamic mixer so as to provide a second hydrocarbon in water emulsion having a second average droplet size; and mixing said first emulsion and said second emulsion so as to provide a final bimodal emulsion. 2. The process of claim 1, wherein said liquid additive comprises at least one surfactant selected from the group consisting of nonionic surfactants, anionic surfactant, natural surfactants, activating additives for activating inactive surfactants and combinations thereof.3. The process of claim 2, wherein said liquid additive comprises an activating additive, and said activating additive is a pH buffer solution selected so as to provide said solution with a pH of at least about 10.4. The process of claim 2, wherein said liquid additive comprises an activating additive, and said activating additive is an alkaline additive selected from the group consisting of sodium, potassium and lithium hydroxides and carbonates, amines and combinations thereof.5. The process of claim 1, wherein said hydrocarbon is selected from the group consisting of crude oil, viscous hydrocarbon, refinery resid, natural bitumen and mixtures thereof, having an API gravity of at least about 5.6. The process of claim 1, wherein said final bimodal emulsion has a hydrocarbon to water ratio greater than 60:40 v/v, with said first average droplet size being about 20 microns and said second average droplet size being about 3 microns.7. The process of claim 1, wherein said bimodal emulsion has two distinct droplet size populations.