US2017369791A1PendingUtilityA1

Crude Quality Enhancement by Simultaneous Crude Stabilization, Sweetening, and Desalting Via Microwave Assisted Heating

Assignee: SAUDI ARABIAN OIL COPriority: Jun 28, 2016Filed: Jun 28, 2017Published: Dec 28, 2017
Est. expiryJun 28, 2036(~9.9 yrs left)· nominal 20-yr term from priority
C10G 33/04C10G 2300/205C10G 31/08C10G 2300/805C10G 31/06C10G 32/02F24H 2250/12C10G 2300/207C10G 33/00
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Claims

Abstract

Embodiments of the disclosure include processes using microwave heating to promote the separation of components of crude oil. In some embodiments, microwave-heated water may be used to heat the interphase between the gas phase and the oil phase of a crude oil stream to promote the separation of sulfur (for example, H 2 S) and light end components of the crude oil stream. In some embodiments, microwave-heated water may be used to heat the interphase between the oil phase and the water phase of a crude oil stream to promote the separation of water, salt, or both of the crude oil stream. Systems having a microwave unit to provide microwave-heated water to crude oil stream are also provided.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A method of processing crude oil, comprising:
 irradiating water at a first temperature with microwaves to produce heated water at a second temperature, the second temperature greater than the first temperature;   providing the heated water to a crude oil stream, the crude oil stream comprising a gas phase, an oil phase, and a water phase; and   providing the crude oil stream to a downstream crude oil processing unit.   
     
     
         2 . The method of  claim 1 , wherein providing the heated water to the crude oil stream comprises directing the heated water at a gas-oil interphase of the crude oil stream. 
     
     
         3 . The method of  claim 1 , wherein providing the heated water to the crude oil stream comprises:
 directing a first portion of the heated water at a gas-oil interphase of the crude oil stream; and   directing a second portion of the heated water at an oil-water interphase of the crude oil stream.   
     
     
         4 . The method of  claim 3 , comprising disrupting an oil-water emulsion using the second portion of the heated water. 
     
     
         5 . The method of  claim 1 , comprising obtaining the water at the first temperature from the crude oil stream. 
     
     
         6 . The method of  claim 5 , comprising separating solids from the water before irradiating the water with microwaves to produce the heated water at the second temperature. 
     
     
         7 . The method of  claim 1 , wherein the water comprises treated water from a water treatment unit of a crude oil processing plant. 
     
     
         8 . The method of  claim 1 , wherein the crude oil processing unit comprises a high pressure production trap (HPPT), a low pressure production trap (LPPT), a stabilization unit, a desalter, or a dehydrator. 
     
     
         9 . The method of  claim 1 , comprising producing a gas stream and a separated crude oil stream from the crude oil processing unit. 
     
     
         10 . The method of  claim 1 , comprising boiling an H 2 S component of the crude oil stream using the heated water. 
     
     
         11 . The method of  claim 1 , comprising boiling light end components of the crude oil stream using the heated water. 
     
     
         12 . The method of  claim 1 , wherein the microwaves have a frequency of 915 MHz. 
     
     
         13 . The method of  claim 1 , wherein the second temperature comprises 194° F. to 250° F. 
     
     
         14 . A system, comprising:
 a pipe configured to transport a crude oil stream to a crude oil processing unit; and   a microwave unit upstream from the crude oil processing unit and coupled to the pipe, the microwave unit configured to:   receive water at a first temperature from the crude oil stream; and,   irradiate the water to produce heated water at a second temperature, wherein the second temperature is greater than the first temperature;   wherein an outlet of the microwave unit is coupled to an inlet of the pipe, the inlet configured to direct the heated water at an oil-gas interphase of the crude oil stream.   
     
     
         15 . The system of  claim 14 , comprising a solids separator coupled to the microwave unit, the solids separator configured to separate solids from the water before the microwave unit receives the water. 
     
     
         16 . The system of  claim 14 , wherein the crude oil processing unit comprises a high pressure production trap (HPPT), a low pressure production trap (LPPT), or a stabilization unit. 
     
     
         17 . The system of  claim 14 , wherein the crude oil stream comprises a first crude oil stream having a first composition, and wherein the crude oil processing unit is configured to output a second crude oil stream having a second composition. 
     
     
         18 . The system of  claim 14 , comprising:
 a crude oil analyzer configured to determine at least one parameter of the second crude oil stream;   a controller configured to:
 receive the at least one parameter from the crude oil analyzer; 
 compare the at least one parameter to a respective at least one threshold value; and 
 modify a power of the microwaves based on the comparison. 
   
     
     
         19 . The system of  claim 18 , wherein the at least one parameter comprises H 2 S content, salt content, or Reid vapor pressure. 
     
     
         20 . A system, comprising:
 a pipe configured to provide a crude oil stream to a crude oil processing unit; and   a microwave unit upstream of the crude oil processing unit and coupled to the pipe, the microwave unit configured to irradiate water at a first temperature to produce heated water at a second temperature, wherein the second temperature is greater than the first temperature;   wherein an outlet of the microwave unit is coupled to a first inlet of the pipe, the first inlet configured to direct a first portion of the heated water at an oil-gas interphase of the crude oil stream;   wherein the outlet of the microwave unit is further coupled to a second inlet of the pipe, the second inlet configured to direct a second portion of the heated water at an oil-water interphase of the crude oil stream.   
     
     
         21 . The system of  claim 20 , wherein the water comprises treated water from a water treatment unit. 
     
     
         22 . The system of  claim 20 , wherein the crude oil processing unit comprises a desalter or a dehydrator. 
     
     
         23 . The system of  claim 20 , wherein the crude oil stream comprises a first crude oil stream having a first composition, and wherein crude oil processing unit is configured to output a second crude oil stream having a second composition. 
     
     
         24 . The system of  claim 20 , comprising:
 a crude oil analyzer configured to determine at least one parameter of the second crude oil stream;   a controller configured to:
 receive the at least one parameter from the crude oil analyzer; 
 compare the at least one parameter to a respective at least one threshold value; 
 modify a power of the microwaves based on the comparison. 
   
     
     
         25 . The system of  claim 24 , wherein the at least one parameter comprises H 2 S content, salt content, or Reid vapor pressure.

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