US2017321537A1PendingUtilityA1

Calculating Static Bottomhole Pressures for Dry and Wet Gas Wells

Assignee: SAUDI ARABIAN OIL COPriority: May 5, 2016Filed: May 5, 2016Published: Nov 9, 2017
Est. expiryMay 5, 2036(~9.7 yrs left)· nominal 20-yr term from priority
E21B 41/00E21B 47/065E21B 47/06E21B 47/07E21B 43/00
34
PatentIndex Score
0
Cited by
0
References
0
Claims

Abstract

A wellbore is divided into a plurality of depth intervals. For each depth interval of the plurality of depth intervals, a specific gas gravity, pseudo-critical gas properties, a pseudo-reduced gas pressure and temperature, a gas deviation factor, and a gas gradient and a bottom node pressure are determined. The determined bottom node pressure is used as a static bottomhole pressure.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A computer-implemented method, comprising:
 dividing a wellbore into a plurality of depth intervals;   for each depth interval of the plurality of depth intervals:
 determining a specific gas gravity; 
 determining pseudo-critical gas properties; 
 determining a pseudo-reduced gas pressure and temperature; 
 determining a gas deviation factor using the pseudo-reduced gas properties; and 
 determining a gas gradient and a bottom node pressure; and 
   using the determined bottom node pressure as a static bottomhole pressure.   
     
     
         2 . The computer-implemented method of  claim 1 , wherein determining the specific gas gravity includes using an equation given by: 
       
         
           
             
               
                 
                   γ 
                   g 
                 
                 = 
                 
                   
                     
                       M 
                       a 
                     
                     
                       M 
                       air 
                     
                   
                   = 
                   
                     
                       M 
                       a 
                     
                     28.97 
                   
                 
               
               , 
             
           
         
       
       and wherein γ g  is the gas specific gravity, M a  is apparent mass, and M air  is the molecular weight of air. 
     
     
         3 . The computer-implemented method of  claim 1 , wherein determining the pseudo-critical gas properties includes using equations given by:
     P   pch =756.8−131.0γ h −3.6γ h   2  
     and       T   pch =169.2+349.5γ h −74.0γ h   2 ,
   
       and wherein P pch  is the pseudocritical pressure of hydrocarbon components, T pch  is the pseudocritical temperature of hydrocarbon components, and γ h  is the specific gravity of hydrocarbon components. 
     
     
         4 . The computer-implemented method of  claim 1 , wherein determining the pseudo-reduced gas pressure and temperature includes using equations given by:
     Ppr=p/Ppc        and       Tpr=T/Tpc,      
       and wherein Ppr is pseudo-reduced pressure, Ppc is pseudocritical pressure, Tpr is pseudo-reduced temperature, Tpc is pseudocritical temperature, p is pressure, and T is temperature. 
     
     
         5 . The computer-implemented method of  claim 1 , wherein determining the gas gradient and the bottom node pressure includes using an equation given by: 
       
         
           
             
               
                 
                   α 
                   g 
                 
                 = 
                 
                   
                     
                       ρ 
                       g 
                     
                     144 
                   
                   = 
                   
                     
                       PMM 
                       a 
                     
                     
                       144 
                        
                       
                           
                       
                        
                       ZRT 
                     
                   
                 
               
               , 
             
           
         
       
       and wherein ρ g  is gas density, P is pressure, m is mass, α g  is the gas wellbore pressure gradient, R is the Universal Gas Constant, T is temperature, and Z is compressibility factor. 
     
     
         6 . A non-transitory, computer-readable medium storing computer-readable instructions executable by a computer and configured to:
 divide a wellbore into plurality of depth intervals;   for each depth interval of the plurality of depth intervals:
 determine a specific gas gravity; 
 determine pseudo-critical gas properties; 
 determine a pseudo-reduced gas pressure and temperature; 
 determine a gas deviation factor using the pseudo-reduced gas properties; and 
 determine a gas gradient and a bottom node pressure; and 
   use the determined bottom node pressure as a static bottomhole pressure.   
     
     
         7 . The non-transitory, computer-readable medium of  claim 6 , wherein determining the specific gas gravity includes using an equation given by: 
       
         
           
             
               
                 
                   γ 
                   g 
                 
                 = 
                 
                   
                     
                       M 
                       a 
                     
                     
                       M 
                       air 
                     
                   
                   = 
                   
                     
                       M 
                       a 
                     
                     28.97 
                   
                 
               
               , 
             
           
         
       
       and wherein γ g  is the gas specific gravity, M a  is apparent mass, and M air  is the molecular weight of air. 
     
     
         8 . The non-transitory, computer-readable medium of  claim 6 , wherein determining the pseudo-critical gas properties includes using equations given by:
     P   pch =756.8−131.0γ h −3.6 h   2  
     and       T   pch =169.2+349.5γ h −74.0γ h   2 ,
   
       and wherein P pch  is the pseudocritical pressure of hydrocarbon components, T pch  is the pseudocritical temperature of hydrocarbon components, and γ h  is the specific gravity of hydrocarbon components. 
     
     
         9 . The non-transitory, computer-readable medium of  claim 6 , wherein determining the pseudo-reduced gas pressure and temperature includes using equations given by:
     Ppr=p/Ppc        and       Tpr=T/Tpc,      
       and wherein Ppr is pseudo-reduced pressure, Ppc is pseudocritical pressure, Tpr is pseudo-reduced temperature, Tpc is pseudocritical temperature, p is pressure, and T is temperature. 
     
     
         10 . The non-transitory, computer-readable medium of  claim 6 , wherein determining the gas gradient and the bottom node pressure includes using an equation given by: 
       
         
           
             
               
                 
                   α 
                   g 
                 
                 = 
                 
                   
                     
                       ρ 
                       g 
                     
                     144 
                   
                   = 
                   
                     
                       PMM 
                       a 
                     
                     
                       144 
                        
                       
                           
                       
                        
                       ZRT 
                     
                   
                 
               
               , 
             
           
         
       
       and wherein ρ g  is gas density, P is pressure, m is mass, α g  is the gas wellbore pressure gradient, R is the Universal Gas Constant, T is temperature, and Z is compressibility factor. 
     
     
         11 . A computer-implemented system, comprising:
 at least one computer interoperably coupled with a memory storage and configured to:
 divide a wellbore into plurality of depth intervals; 
 for each depth interval of the plurality of depth intervals:
 determine a specific gas gravity; 
 determine pseudo-critical gas properties; 
 determine a pseudo-reduced gas pressure and temperature; 
 determine a gas deviation factor using the pseudo-reduced gas properties; and 
 determine a gas gradient and a bottom node pressure; and 
 
 use the determined bottom node pressure as a static bottomhole pressure. 
   
     
     
         12 . The computer-implemented system of  claim 11 , wherein determining the specific gas gravity includes using an equation given by: 
       
         
           
             
               
                 
                   γ 
                   g 
                 
                 = 
                 
                   
                     
                       M 
                       a 
                     
                     
                       M 
                       air 
                     
                   
                   = 
                   
                     
                       M 
                       a 
                     
                     28.97 
                   
                 
               
               , 
             
           
         
       
       and wherein γ g  is the gas specific gravity, M a  is apparent mass, and M air  is the molecular weight of air. 
     
     
         13 . The computer-implemented system of  claim 11 , wherein determining the pseudo-critical gas properties includes using equations given by:
     P   pch 756.8−131.0γ h −3.6γ h   2  
     and       T   pch =169.2+349.5γ h −74.0γ h   2 ,
   
       and wherein P pch  is the pseudocritical pressure of hydrocarbon components, T pch  is the pseudocritical temperature of hydrocarbon components, and γ h  is the specific gravity of hydrocarbon components. 
     
     
         14 . The computer-implemented system of  claim 11 , wherein determining the pseudo-reduced gas pressure and temperature includes using equations given by:
     Ppr=p/Ppc        and       Tpr=T/Tpc,      
       and wherein Ppr is pseudo-reduced pressure, Ppc is pseudocritical pressure, Tpr is pseudo-reduced temperature, Tpc is pseudocritical temperature, p is pressure, and T is temperature. 
     
     
         15 . The computer-implemented system of  claim 11 , wherein determining the gas gradient and the bottom node pressure includes using an equation given by: 
       
         
           
             
               
                 
                   α 
                   g 
                 
                 = 
                 
                   
                     
                       ρ 
                       g 
                     
                     144 
                   
                   = 
                   
                     
                       PMM 
                       a 
                     
                     
                       144 
                        
                       
                           
                       
                        
                       ZRT 
                     
                   
                 
               
               , 
             
           
         
       
       and wherein ρ g  is gas density, P is pressure, m is mass, α g  is the gas wellbore pressure gradient, R is the Universal Gas Constant, T is temperature, and Z is compressibility factor.

Join the waitlist — get patent alerts

Track US2017321537A1 — get alerts on status changes and closely related new filings.

We store only your email — no account needed. See our privacy policy.