US2020124273A1PendingUtilityA1

Separators and mixers for delivering controlled-quality solar-generated steam over long distances for enhanced oil recovery, and associated systems and methods

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Assignee: GLASSPOINT SOLAR INCPriority: Feb 1, 2016Filed: Jun 5, 2019Published: Apr 23, 2020
Est. expiryFeb 1, 2036(~9.6 yrs left)· nominal 20-yr term from priority
F22B 1/22F22B 1/006E21B 43/24F22B 37/26F01K 3/242Y02P80/154Y02P80/15
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Claims

Abstract

Separators and mixers for delivering controlled-quality solar-generated steam over long distances for enhanced oil recovery, and associated systems and methods. A representative method includes heating water to steam at a solar field, separating a liquid fraction from the steam, directing the steam toward a target steam user via a first, steam conduit, and directing the liquid fraction toward the target steam user in parallel with the steam via second, liquid fraction conduit. The method can further include mixing the liquid fraction and the steam before delivering the combined liquid fraction and steam to the target user.

Claims

exact text as granted — not AI-modified
I/We claim: 
     
         1 . A method for providing solar-heated steam to a target user, comprising:
 heating water to steam at a solar field;   separating a liquid fraction from the steam;   directing a vapor fraction of the steam toward the target user via a first, vapor fraction conduit; and   directing the liquid fraction toward the target user in parallel with the vapor fraction via a second, liquid fraction conduit.   
     
     
         2 . The method of  claim 1 , further comprising mixing the at least part of the liquid fraction and at least part of the vapor fraction to form a steam mixture, before delivering the steam mixture to the target user. 
     
     
         3 . The method of  claim 1 , further comprising disposing of the liquid fraction without mixing at least part of the liquid fraction and at least part of the vapor fraction to form a steam mixture. 
     
     
         4 . The method of  claim 1 , further comprising:
 mixing at least part of the liquid fraction with additional liquid water at the target user to form a water mixture; and   disposing of the water mixture.   
     
     
         5 . The method of  claim 1  wherein the solar field includes at least one receiver carrying water, and at least one concentrator positioned to concentrate solar radiation on the at least one receiver. 
     
     
         6 . The method of  claim 1  wherein the vapor fraction is dry, non-superheated steam. 
     
     
         7 . The method of  claim 1  wherein the vapor fraction has a quality of 95% or higher upon separation. 
     
     
         8 . The method of  claim 1  wherein the vapor fraction has a quality of 90% or higher immediately prior to mixing. 
     
     
         9 . The method of  claim 1  wherein the solar field is a first solar field, and wherein the method further comprises:
 after a period of time, changing a state of a second solar field from a non-operational state to an operational state; and 
 with both the first and second solar fields in an operational state:
 directing vapor fractions from both the first and second solar fields toward the user via the vapor fraction conduit; and 
 directing liquid fractions from both the first and second solar fields toward the user via the liquid fraction conduit. 
 
 
     
     
         10 . The method of  claim 1  wherein heating water to steam includes heating water to steam at a first rate and a second rate that is at least seven times the first rate, and wherein directing the vapor fraction includes directing the vapor fraction at both the first and second rates without separating liquid from vapor in the vapor fraction conduit. 
     
     
         11 . The method of  claim 1  wherein a flow rate of the vapor fraction varies from a first rate to a second rate at least 28 times the first rate, and wherein directing the vapor fraction includes directing the vapor fraction at both the first and second rates without separating liquid from vapor in the vapor fraction conduit. 
     
     
         12 . The method of  claim 1 , further comprising draining liquid from the liquid fraction conduit when the solar field is inactive. 
     
     
         13 . A solar steam generation system, comprising:
 a solar field having a water inlet and a steam outlet;   a separator coupled to the steam outlet to separate a liquid fraction from steam received from the steam outlet;   a vapor fraction conduit coupled to the separator to receive a vapor fraction from the separator, the vapor fraction conduit being positioned between the separator and a target steam user; and   a liquid fraction conduit coupled to the separator in parallel with the vapor fraction conduit to receive the liquid fraction from the separator, the liquid fraction conduit being positioned between the separator and the target steam user.   
     
     
         14 . The system of  claim 13 , further comprising:
 a mixer coupled to the vapor fraction conduit and the liquid fraction conduit downstream of the separator and upstream of the target steam user to receive and mix the steam and liquid fraction; and   a target user supply conduit coupled between the mixer and the target steam user.   
     
     
         15 . The system of  claim 13 , further comprising a controller operatively coupled to the vapor fraction conduit and the liquid fraction conduit, and programmed with instructions that, when executed:
 direct steam from the user toward the separator via the vapor fraction conduit when the solar field is inactive.   
     
     
         16 . The system of  claim 13 , further comprising a controller operatively coupled to the vapor fraction conduit and the liquid fraction conduit, and programmed with instructions that, when executed:
 direct steam from the user toward the separator via the liquid fraction conduit when the solar field is inactive.   
     
     
         17 . The system of  claim 13  wherein the user is spaced apart from the separator by a distance of at least 200 meters. 
     
     
         18 . The system of  claim 13  wherein the user is spaced apart from the separator by a distance of at least 500 meters. 
     
     
         19 . The system of  claim 13  wherein the user is spaced apart from the separator by a distance of at least 1000 meters. 
     
     
         20 . The system of  claim 13  wherein the target user includes an enhanced oil recovery facility. 
     
     
         21 . The system of  claim 13 , further comprising:
 a mixer coupled to the vapor fraction conduit and the liquid fraction conduit downstream of the separator and upstream of the target steam user to receive and mix the steam and liquid fraction;   two headers coupled to and positioned downstream of the mixer; and   a plurality of fluid conduits coupled in parallel between the two headers.   
     
     
         22 . The system of  claim 21  wherein the fluid conduits are sized to produce or maintain turbulent flow.

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