PROCESS FOR TREATING HEAVY OILS

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PROCESS FOR TREATING HEAVY OILS ( process-for-treating-heavy-oils )

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13 32. The process of claim 31 wherein said organic material ispentane. 33. The process of claim 30 Wherein said heavy oil and an organic material are mixed in a mixing Zone, to provide a mixtureofsaidheavyoilandsaidorganicmaterial,andsaid 5 mixture of said heavy oil and said organic material is sub jected to said hydrodynamic cavitation in said cavitation Zone. 34. The process of claim 33 Wherein the Width of said hydrodynamiccavitationZoneislessthantheWidthofsaid 10 mixing Zone. 35. The process of claim 34 Wherein the ratio of the Width of said hydrodynamic cavitation Zone to the Width of said mixing Zone is from about 1/230 to about 1/75. 36. The process of claim 33 Wherein, prior to mixing said heavyoilWithsaidorganicmaterial,saidheavyoilisheated to a temperature of from about 75° C. to about 450° C., and saidorganicmaterialisheatedtoatemperatureoffromabout 75° C. to about 800° C. 37.Theprocessofclaim36Whereinsaidheavyoilis20 heated to a temperature of from about 150° C. to about 450° C. 14 46. The process of claim 30 Wherein said liquid is passed through said cavitation Zone at a velocity of from about 100 m/ sec to about 300 m/ sec, and is subjected to a pressure drop of from about 150 psi to about 5,000 psi. 47. The process of claim 46 Wherein said liquid is passed through said cavitation Zone at a velocity of from about 150 m/sec to about 300 m/ sec. 48. The process of claim 47 Wherein said liquid is passed through said cavitation Zone at a velocity of from about 200 m/sec to about 300 m/ sec. 49.Theprocessofclaim46Whereinsaidliquidissubjected toapressuredropoffromabout400psigtoabout4,000psig. 50.Theprocessofclaim49Whereinsaidliquidissubjected toapressuredropoffromabout400psigtoabout2,000psig. 51.Theprocessofclaim50Whereinsaidliquidissubjected toapressuredropoffromabout400psigtoabout1,500psig. 52.Theprocessofclaim51Whereinsaidliquidissubjected to a pressure drop of from about 1,000 psig to about 1,500 psig. 53. The process of claim 30 Wherein the ratio of the length of the cavitation Zone to the Width of the cavitation Zone is from about 10 to about 125. 54. The process of claim 53 Wherein the ratio of the length ofthecavitationZonetotheWidthofthecavitationZoneis from about 50 to about 125. 55.A processfortreatingaheavyoil,comprising: mixing a heavy oil, and an organic material other than a heavy oil in a mixing Zone, Wherein each of said heavy oil and said organic material is a liquid at standard tem perature and pressure, to provide a feed Which consists essentiallyofaliquidatstandardtemperatureandpres sure; passingsaidfeedthroughahydrodynamiccavitationZone, Wherein the ratio of the Width of said cavitation Zone to the Width of said mixing Zone is from about 1/230 to about 1/75, and ratio of the length of said caviation Zone to the Width of said cavitation Zone is from about 10 to about 125, Wherein a portion of the liquid Which is passed through said cavitation Zone is formed into microbubblesdispersedinsaidliquid,Wherebysaidliq uid is subjected to hydrodynamic cavitation to reduce theviscosityofsaidheavyoil. 38. The process of claim 37 Wherein said heavy oil is heated to a temperature of from about 200° C. to about 450° C. 39. The process of claim 38 Wherein said heavy oil is heated to a temperature of from about 200° C. to about 400° C. 25 40. The process of claim 39 Wherein said heavy oil is heatedtoatemperatureoffromabout300°C.toabout400° 30 C. 41.Theprocessofclaim36Whereinsaidorganicmaterial isheated to a temperature offrom about 150° C. to about 800° C. 42.Theprocessofclaim41Wheresaidorganicmaterialis 35 heated to a temperature of from about 300° C. to about 800° C. 43. The process of claim 42 Wherein said organic material isheated to a temperature offrom about 300° C. to about 600° C. 44. The process of claim 43 Wherein said organic material isheated to a temperature offrom about 300° C. to about 400° C. 40 45. The process of claim 30 Wherein said organic material ispresentinsaidliquidinanamountoffromabout5vol.% 45 toabout25vol.% ofthevolumeofsaidheavyoil. US 8,105,480B2

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