US 20020116986 A1 Abstract A method and apparatus for locating leaks at an undetermined location in a section of pipeline of known length. Standard pressure vessels of relatively small volume are connected to respective ends of the pipeline section through valves. The pipeline is closed at each end and the valves into the standard pressure vessels are opened. Fluids are placed in the pipeline under a pressure. The valves to both of the standard pressure vessels are simultaneously closed, isolating each of the standard pressure vessels from the pipeline section so as to maintain the pressure vessels at substantially the same level as at the time of closing. The differential pressure between each end of the pipeline and its respective standard pressure vessel is then continuously monitored and recorded in real time measurements. The location of a leak is determined by solving an equation, based on the equilibrium equation and real time measured differential pressure values at each end of the pipeline.
Claims(15) 1. A method of locating leaks at an undetermined location in a section of pipeline of known length comprising the steps of:
providing at each end of said section of pipeline a standard pressure vessel of relatively small volume; connecting each of said standard pressure vessels to a respective end of said pipeline section through a respective valve; closing each end of said section of pipeline and opening said valves into said standard pressure vessels; assuring that fluids in said section of pipeline and in said standard pressure vessels are under a pressure of at least a predetermined level; simultaneously closing each of said standard pressure vessel valves isolating each of said standard pressure vessels from said section of pipeline; continuously monitoring and recording, in real time measurements, the differential pressure between each end of said pipeline and its respective standard pressure vessel; and determining the location of said leak by solving the following equation: DP(−A,t _{1})/DP(B,t _{1})=Cosh(A)/Cosh(L-A) where DP(−A,t,)=differential pressure between one end of said pipeline section and its respective standard pressure vessel at time t _{1}; DP(B,t _{1})=differential pressure between the opposite end of said pipeline section and its respective standard pressure vessel at time t_{1}; L=the known length of said pipeline section; and A=the distance between said one end of said pipeline section and the location of said leak. 2. The method of locating pipeline leaks as set forth in 3. The method of locating pipeline leaks as set forth in 4. The method of locating pipeline leaks as set forth in 5. The method of locating pipeline leaks as set forth in 6. The method of locating a pipeline leak as set forth in 7. The method of locating a pipeline leak as set forth in 8. The method of locating a pipeline leak as set forth in 9. Apparatus for locating leaks at an undetermined location in a section of pipeline of known length, the ends of which may be closed, said apparatus comprising:
a first standard pressure vessel of relatively small volume at one end of said pipeline section, a second standard pressure vessel substantially identical to said first standard pressure vessel at the opposite end of said pipeline section; each of said first and second pressure vessels being in fluid communication with said one and said opposite ends of said pipeline section, respectively, through a first conduit and valve and a second conduit and valve, respectively; each of said first and second valves being simultaneously closeable to isolate each of said first and second standard vessels from their respective ends of said pipeline section; first differential pressure measuring means connected to said one end of said pipeline section and said first standard pressure vessel for measuring the differential pressure therebetween; and second differential pressure means connected to said opposite end of said pipeline section and said second standard pressure vessel for measuring the differential pressure therebetween. 10. Pipeline leak locating apparatus as set forth in 11. Pipeline leak detecting apparatus as set forth in 12. Pipeline leak detecting apparatus as set forth in DP(−A,t _{1})/DP(B,t _{1})=Cosh(A)/Cosh(L−A) where DP(−A,t
_{1})=differential pressure between one end of said pipeline section and its respective standard pressure vessel at time t_{1};
DP(B,t
_{1})=differential pressure between the opposite end of said pipeline section and its respective standard pressure vessel at time t_{1}; L=the known length of said pipeline section; and
A=the distance between said one end of said pipeline section and the location of said leak.
13. Pipeline leak locating apparatus as set forth in 14. Pipeline leak locating apparatus as set forth in 15. Pipeline leak locating apparatus as set forth in Description [0001] 1. Field of the Invention [0002] The present invention pertains to methods and apparatus for locating leaks in pipelines. More specifically, the present invention pertains to methods and apparatus for locating small fluid leaks at undetermined locations in a pipeline, especially those of a magnitude not easily detected by other methods. [0003] 2. Brief Description of the Prior Art [0004] Increased awareness of environmental, safety and financial consequences of petroleum and petroleum products leaking from pipelines has heightened the demand for accurate methods and apparatus for detecting and determining the location of pipeline leaks. Most pipelines are buried in the ground and, unless the leak is large enough to be visible from the surface of the ground or the air, may not be easily detected. This is especially true for very small leaks. Although small leaks may not be as hazardous as large ones, environmental, safety and financial consequences are still of great importance. [0005] The typical method for determining if there is a leak in a pipeline is hydrostatic testing where fluids, such as water, are placed in the section of pipeline under observation. The pipeline section is closed at both ends and the fluids are pressurized therein. Pressure and temperature measuring devices are monitored over the next several hours to indicate whether there is a leak or not. However, even though declining pressure may indicate a leak, a leak may be so small as not to be readily located. [0006] A number of pressure, volume and flow measuring techniques have been developed for determining and locating leaks in pipelines. However, none of them appear to be totally effective in accurately locating very small pipeline leaks. The industry continues to search for more effective and efficient methods and apparatus for doing so. [0007] The present invention provides a method and apparatus for locating leaks at an undetermined location in a section of pipeline of known length. A standard pressure vessel of relatively small volume is provided at each end of the pipeline section and connected to respective ends of the pipeline section through a valve. The section of pipeline is closed at each end and the valves into the standard pressure vessels are opened. Fluids, whether they be water or other fluids, are placed in the pipeline and the standard pressure vessels under a pressure of at least a predetermined level. Then the valves to both of the standard pressure vessels are simultaneously closed, isolating each of the standard pressure vessels from the pipeline section so as to maintain the pressure vessels at substantially the same level as at the time of closing. The differential pressure between each end of the pipeline and its respective standard pressure vessel is then continuously monitored and recorded in real time measurements and, if there is a leak, the location of the leak is determined by solving an equation, based on the equilibrium equation and real time measured differential pressure values at each end of the pipeline. [0008] Apparatus for performing the method of the present invention includes, in addition to the standard pressure vessels and associated valves at each end of the pipeline, differential pressure measuring means at each end of the pipeline and means for continuously monitoring and recording the differential pressures. In a preferred embodiment, the apparatus includes a computer which is programmed to solve an equation for determining the distance of a leak from one end of the pipeline section by utilizing the real time measured differential pressures. Preferred embodiments also include transmitters operatively connected to the differential pressure means at each end of the pipeline and a receiver remotely located with and connected to the computer to effect simultaneous real time input from the differential pressure means at both ends of the pipeline section for processing by the computer. [0009] With the method and apparatus of the present invention, the location of a leak can be accurately determined within a relatively short period of time. The apparatus for performing the method requires accurate instruments. However such instruments are readily available with today's technology. The components of the apparatus are simply configured, installed and operated. Other objects and advantages of the invention will be apparent from reading the description which follows in conjunction with the accompanying drawings. [0010]FIG. 1 is a drawing schematically representing a pipeline section having a leak therein and illustrating apparatus of the present invention used in determining the location of the leak; [0011]FIG. 2 is a graph representing fluid pressure in the pipeline at various locations; and [0012]FIG. 3 is a schematic representation of apparatus utilized in the method of the present invention. [0013] Referring first to FIG. 1, there is represented a section of pipeline [0014] Provided at each end of the pipeline are first and second “standard” pressure vessels [0015] Each end [0016] Each end [0017]FIG. 3 is a schematic representation, in block form, which further illustrates the method and apparatus of the present invention. The pipeline section [0018] Also shown and represented in FIG. 3 is a receiver [0019] The computer processor solves an equation: [0020] where: [0021] DP(−A,t [0022] DP(B,t [0023] L=known length of pipeline section [0024] A=the distance between one end [0025] B=the distance between the opposite end [0026] With this equation the leak [0027] The magnitude of the flow velocity in a pipeline from a small leak, is nil. The kinetic energy of the flow is essentially zero; therefore, conventional hydraulic methods are not suitable for finding very small leaks. [0028] When a pipeline is pressurized, the pipeline and its medium are compressed (strained and stressed). A great deal of elastic strain energy is stored in the pipe. Strained compressive energy is also stored in the medium itself (fluid or gas), including thermal energy. By suddenly opening a valve in a pipeline, this stored energy is released to produce water-hammer. The stored (potential) energy is then converted to kinetic energy and then back to potential energy, surging several times to produce a devastating and destructive effect on the pipeline. [0029] When a small leak occurs in the pipeline the compressed energy is released slowly. The method of locating the leak of the present invention is based on the relatively slow release of this stored energy. By obtaining and recording very precise pressure drop readings at recorded time intervals, the constants of the equation which describe the internal pressure of the fluid or gas contained in the pipeline as it varies with both distance along the pipe and with time can be experimentally determined. By obtaining the pressure variation equation, all the energies and deformations of the pipeline and its medium can be determined, including the magnitude of the leak rate. [0030] The internal pressure equation utilized in the present invention is derived from the general equilibrium equation which is applicable for any medium, be it a solid elastic medium such as the pipe itself or its internal medium, the fluid or gas that it contains. [0031] The Equilibrium Equation ∇·σρ [0032] Definitions [0033] [M]=Mass [L]=Length [T]=Time
[0034] For a perfect fluid or gas the stress tensor is equal to: σ=−PI Equation No. 2 [0035] where P is equal to pressure and I is the unity tensor. [0036] Pressure is equal to: [0037] where B is the bulk modulus of the fluid or gas and ∇·μ is the divergence of the displacement field. [0038] Substituting Equation No. 2 in Equation No. 1 we get: −∇ [0039] Taking the divergence of Equation No. 4, ∇·[−∇ [0040] −∇ B/ρ=α [0041] where α equals the speed of sound in the medium. [0042] If ∇·(ρf)=0, which is the case for a gravity field near the surface of the earth, we are left with the equation: ∇ [0043] In cylindrical coordinates, this is: ∂ [0044] Since the Pressure in the fluid or gas in the pipeline does not vary in this case, in the radial (r) or circular (e) direction, the pressure is a function of time (t) and of distance (z) only. Placing the z coordinate along the center line of the pipeline: ∂ P=P(z,t) [0045] Letting the pressure function be the product of two functions, distance Z and time T(times a constant), P=Z·T, and substituting into Equation No. 6 [0046] Separating variables by dividing both sides by (Z·T) (1 [0047] is a constant. If the sign in front of λ [0048] The Z general function of distance is equal to: [0049] The T general function of time is equal to: [0050] Equation No. 4 requires the consideration of pressure variation along the pipeline due to the earth's gravity field. This pressure variation is constant with time but varies linearly with distance due to elevation changes. Finally, there is pressure constant required to account for atmospheric pressure. For example, if the pipeline were perfectly level and the leak were to occur on top of a pipeline full of liquid, only a small amount of the liquid would spill out. The pressure of the pipeline would drop only to atmospheric pressure and the pipeline would remain virtually full. [0051] The complete general pressure equation, therefore, is: [0052] Now, we must look at the physics of the problem to determine the boundary conditions. First, after a leak occurs, the internal pressure decreases with time, it does not increase. Therefore, constant C [0053] Mathematically, minimum pressure means that: ∂ ∂ [0054] For z=0 at the leak ∂ [0055] For [C [0056] The final working general pressure equation we are left with then is: [0057] Before detailing the method for mathematically locating a pipeline leak using Equation No. 9 accuracy of the pressure reading should be discussed. As valuable and essential as equation No. 9 is, it is only as accurate as the variables used in the equation. The key variables in Equation No. 9 are pressure and time. [0058] The electronic clocks of computers for logging the data are highly accurate. At this time there is no need to get any more accurate. The accuracy of the pressure readings is another case. Present state-of-the-art electronic instrumentation is usually +/− 0.5% inaccuracy over the range of the operation. For example, if the hydrostatic test pressure of a pipeline is 950 psig, and a test pressure gauge of 1200 psig range is used, the accuracy of the gauge is: 1200 psig×0.5/100=+/−6.0 psig. [0059] It is obvious (from uncertainty analysis of the equation) that very accurate pressure readings are needed. Toward this goal, the “standard” pressure vessels [0060] In order to increase accuracy of pressure readings, differential pressures measured in inches of water are taken relative to a fixed “standard” pressure. At each end [0061] The location of the leak will now be shown using Equation No. 9 which is here repeated: [0062] Let us chose the origin of the coordinate system to be at the leak [0063] After the pumping stops and the pressure of the pipeline section starts to drop, due to the leak, the pressure in each standard pressure vessel [0064] At zero datum time, at Station [0065] First, let C [0066] At a later time t [0067] By subtracting Eq. No. 11 from Eq. No. 10, we have: [0068] Doing the same thing for another differential pressure reading at another time interval t [0069] Dividing Eq. No. 12 by Eq. No. 13 we finally get: [0070] α is the speed of sound in water and can be experimentally determined from the temperature readings taken. Therefore, from Eq. 14, λ can be mathematically determined. λ is a characteristic of the pipeline and could just as easily have been determined at Station [0071] After λ has been determined, differential pressures taken at the same time, at each Station [0072] Dividing Eq. No. 12 by Eq. no 15 we then have: [0073] Noting that: Cosh(λ(A))=[exp(λ(−A)+exp(−λ(−λ(−A))], Equation No. 16 is then: [0074] L is the total length of the pipeline, and must be known. A+B=L. Substituting L−A for B in Eq. No. 17 we get: [0075] From Eq. 18, A can be mathematically determined. A is the distance from Station [0076] With the method and apparatus of the present invention, leaks of small magnitude can be accurately located and repaired in a relatively short period of time and at reasonable cost. This may result in substantial environmental, safety and financial rewards. [0077] Although a preferred method and apparatus therefor are disclosed herein, many variations may be made by those skilled in the art without departing from the spirit of the invention. Accordingly, it is intended that the scope of the invention be limited only by the claims which follow. Referenced by
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