Abstract:
A method for evaluating wellbore integrity including introducing a drill to a surface of a casing encompassing an annulus, enclosing the drill in a housing hydraulically isolating the surface, drilling through the casing and into cement surrounding the casing, observing a pressure of the fluid, and using the pressure observation and a drill position to evaluate a presence of a defect and a location of the defect. Apparatus for evaluating wellbore integrity including a probe comprising a drill, wherein the probe is hydraulically isolated from the wellbore, a valve that encompasses the drill, a pressure gauge to measure the pressure of the fluid within the housing, a pressure gauge to measure the pressure in the system outside the housing, and equipment to compare the pressure measurements and the position of the drill and to evaluate a presence and a location of the defect.

Description:
FIELD 
     This application relates to methods and apparatus to identify and estimate wellbore isolation characteristics, specifically defects in annular cement between the casing and the formation. 
     BACKGROUND 
     Well-bore zonal isolation is a very important requirement for both geological storage of CO 2 , and oil and gas production. It is a prerequisite for efficient and safe operation. Presence of micro-annuli, isolation defects or poor quality cementing facilitates hydraulic communication, thus allowing fluid migration, and pose a safety and contamination risk. Lack of proper isolation leads to costly treatment facilities, well intervention and operational interruptions. Isolation is achieved by pumping cement through the annulus between the casing and the formation. 
     In CO 2  sequestration and oil and gas wells, estimating the quality of the annular isolation and repairing the cement where necessary is important for preventing potential leaks and fluid contamination. The presence of a mudcake adjacent to the formation and the lack of slip at the walls may lead to unfilled annuli during cementing. Cracks and micro-annuli may also form during setting and shrinkage, and radial cracks may be initiated due to expansion of the casing during pressurization. Such imperfections in cement facilitate inter-zonal migration. Additionally chemical alteration of cement is also complex and depends on thermodynamics, kinetics and diffusion of reactive species leading to reaction fronts. Both mechanical and chemical processes can cause radial and azimuthal variations in the cement properties. The ability to detect the presence of micro-annuli or isolation defects and where possible, quantitatively estimate cement transmissibility is crucial for ensuring project safety. 
     The quality of cement in the annulus is traditionally evaluated by ultrasonic measurements. These measurements, however, provide only qualitative evaluation of hydraulic isolation and are not suitable for volumetric estimation of subtle cement defects or cement transmissibility. 
     Other work has focused on techniques to quantify cement permeability in the annulus. These methods are based on the relationship between the observed pressure and the flow rate through a pressure probe set behind the casing. The flow rate may in turn be expressed in terms of the decompression characteristics of the fluid in the tool. Elimination of the flow rate allows one to obtain an explicit expression for the pressure decay in terms of permeability in the local region around the probe. Significant variation in the permeability estimates obtained at progressive depths of probe penetration within the cemented annulus could be interpreted as an indication of the cement permeability alteration. Although these procedures could be used to detect the changes in hydraulic isolation of the cement sheath, they do not provide any information on the presence and size of the isolation defects—a key input into the remedial action plan. 
     SUMMARY 
     Embodiments relate to apparatus and methods for evaluating wellbore integrity including introducing a drill to a surface of a casing encompassing an annulus, enclosing the drill in a housing hydraulically isolating the surface, drilling through the casing and into cement surrounding the casing, observing a pressure of the fluid within the housing and the annulus, and using the pressure observation and a drill position to evaluate a presence of a defect and a location of the defect. Embodiments also relate to apparatus and methods for evaluating wellbore integrity including a probe comprising a drill, wherein the probe is hydraulically isolated from the wellbore, a valve comprised in a housing that encompasses the drill, a pressure gauge to measure the pressure of the fluid within the housing, a pressure gauge to measure the pressure in the system outside the housing, and equipment to compare the pressure measurements and the position of the drill and to evaluate a presence and a location of the defect. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         FIG. 1  is a schematic diagram of tool components. 
         FIG. 2  is a chart of pressure as a function of time. 
         FIG. 3  is a flow chart of a testing procedure. 
         FIGS. 4A and 4B  are schematic diagrams of (a) geometry of the defect—top view and (b) illustration of the corresponding ultrasonic image—side view. 
     
    
    
     DETAILED DESCRIPTION 
     Motivated by the requirements outlined above, we disclose a tool and technique to detect and quantify the volume of hydraulically well-connected defects within the cemented annulus between the casing and the formation. The terms micro-annulus, crack, cavity are used interchangeably herein. The technique allows for multiple measurements at the same well depth and azimuth and is based on the interpretation of passive pressure measurement from single-probe cased-hole formation testing. Generally, some components of embodiments of this may benefit from concepts described in U.S. Pat. Nos. 7,753,117 and 7,753,118, which are both incorporated by reference herein in their entirety. 
     The technique disclosed herein allows for an almost real-time detection of the isolation defects and provides a method to estimate the volume of a connected region of cement cracks and micro-annuli. These are distinguished from a cement matrix by the large transmissibility of fluids within them, and thus enabling pressure equalization between the probe and the defect in a very short time scale in comparison to the characteristic time of a pretest. 
     The procedure entails the use of a cased-hole formation tester, which allows hydraulic communication with the cement through a probe placed coaxially with a drill assembly. In some embodiments, sudden changes in pressure during drilling are used to detect a micro-annulus. A special procedure is developed to estimate the volume of the micro-annulus supplemented by a profile of cement transmissibility as the probe is placed progressively deeper within the cement interior. 
     The schematic of the tool  100  for micro-annulus detection and quantification is shown on  FIG. 1 . The tool design is based on the Cased Hole Dynamic Tester (CHDT™, commercially available from Schlumberger Technology Corporation of Sugar Land, Tex.) and is a modification thereof. The housing  110  contains a drill bit  111  that is able to drill through the casing into the cemented annulus through the probe  115  assembly. The probe is hydraulically isolated from the wellbore and provides direct hydraulic communication between the flowlines  112 ,  113  of the tool  100  and the cemented annulus through the probe isolation valve  117 . The isolation valve  117  is shown in the figure but the tool may be operated without it. 
     The pressure in the tool flowlines  112 ,  113  is measured by pressure gauges  120  and  130 . The flowline isolation valve  140  controls the flow into the flowline bus  145  for fluid analysis and fluid collection in the storage chambers (not shown). The pretest isolation valve  150  controls the connection of the flowline  113  with the pretest chamber  170 . When equalizing valve  160  is open, the fluid in the tool flowlines  112 ,  113  is exposed to the wellbore pressure. There is a piston  175  in the pretest chamber that controls the drawdown and the pumpout of the fluid from the pretest chamber. Surface circuitry  50  represents control, communication, and preprocessing circuitry for the tool. This circuitry, some of which may be located downhole in the tool itself, may be of known type. A processor  60  and a recorder  70  may also be provided uphole. The circuitry  50 , the processor  60 , and the recorder  70  can communicate with the tool  100  via an armored multi-conductor cable  40 . The testing procedures described below can be performed using a suitably programmed processor (such as a computer, microprocessor or a DSP). The tool  100  includes electronics  45  for at least one of storing, pre-processing, processing, and sending uphole to the surface circuitry  50  information related to pressure sensed by the pressure gauges  120  and  130 . The electronics  45  may have additional functions including: receiving control signals from the surface circuitry  50  and for controlling the piston  175 , controlling the drill  111 , and controlling valves  117 ,  140 ,  150 , and  160 . It will be appreciated that any tool such as the Schlumberger CHDT™ which includes tool-setting pistons, a drill, a hydraulic line and electronics, can be modified, if necessary, with the appropriate sensors and can have its electronics programmed or modified to accomplish the functions of tool  100  as further described below. 
     Testing Procedure 
     In one embodiment, the testing procedure consists of five components:
         Detection of the isolation defect   Evaluation of hydraulic isolation of the defect (connectivity to permeable formation)   Quantification (volume evaluation) of the isolated defect   Volume assignment for a gas-filled defect, if applicable   Evaluation of transmissibility of the isolation defect across zones that need to be isolated from each other
 
Detection of the Isolation Defect
       

     This section discusses the testing procedure to detect the presence of the defects in the cement. It is assumed that the tool  100  is positioned at the depth of interest and the probe  115  is set to hydraulically isolate the flowlines  112 ,  113  of the tool from the wellbore. The flowline isolation valve  140  and the equalizing valve  160  that allows communication to the borehole are initially in the CLOSED position. 
     As is common, it is assumed that the pressure in the cemented annulus is lower than the wellbore pressure. The methods disclosed here are also applicable when the situation is reversed, except that the terminology for pressure decline and increase would be reversed. By opening equalizing valve  160  and pretest isolation valve  150 , the fluid in the tool pretest and the probe lines are exposed to the wellbore pressure. Once the pressure measured at the pressure gauges  120  and  130  reaches the wellbore pressure, the equalizing valve  160  is shut into the closed position. Thus, the measured pressure within the tool is the wellbore pressure. 
     In another embodiment, the equalizing valve  160  is open and the pretest chamber  170  is filled with wellbore fluid. With probe isolation valve  117  and equalizing valve  160  in closed position, the pressure in the tool flowlines  112 ,  113  can be increased to a desired value by decreasing the volume in the pretest chamber  170  by moving the piston  175  forward from a previously retracted position. Caution must be exercised that the pressure does not exceed the wellbore pressure significantly lest a seal between the wellbore and the probe may fail. Conversely, by having the pretest piston retracted by a small amount, the pressure may be decreased. 
     The disclosed defect identification procedure is based on the detecting sudden change in the pressure measured in the part of the tool flowline, which is in hydraulic communication with the probe. The decrease occurs upon fluid pressure communication of the probe with the defect. If the sudden decrease brings the measured tool pressure to the subsequently identified formation pressure, the cement is identified to be a failed one. Any intermediate value is indicative of an isolated defect. For the present purpose, an isolated defect communicates via robustly set cement, the latter exhibiting permeabilities of a few μD or below. 
     After the drill-bit penetrates through the casing into the cemented annulus, it may intersect the micro-annulus or a crack in the cement. Let P t  be the initial pressure in the tool flowline, and P c  the initial pressure in the cement before the start of the test. Once the defect is intersected by the drill-bit, the pressure in the flowline will immediately decrease to a value between P t  and P c  as illustrated on  FIG. 2  (segment  210 ). The drop in the pressure occurs since the fluid in the tool flowlines becomes exposed to the fluid in the cement cavity initially at a lower pressure. Therefore, the pressure in the combined flowline and cavity volume will quickly equilibrate to a new pressure P e . The subsequent decompression to the formation pressure because of the minor communication via the remaining cement is a relatively slow process, as illustrated in  FIG. 2  (segment  220 ). The latter is controlled by the permeability of the cement around the drilled probe and the surface area of the intersected defect. The interpretation procedure (disclosed in U.S. Pat. No. 7,753,118, incorporated by reference herein in a previous application paragraph) with suitable modification can be then applied to estimate the magnitude of effective permeability of the cement. The modification requires consideration of the defect providing a large areal contact of uniform pressure. For this, the new total volume given by the flow-line and the detected defect should be used in the calculation along with an assumed geometry of the defect. The method to estimate the volume of the defect is disclosed in the next section. 
     If the obtained permeability estimate indicates uniform low permeability cement (about a few μD and below) around the defect, the detected anomaly is most likely not directly hydraulically connected to the highly permeable formation zone. Alternatively, if the pressure evolution quickly equilibrates at pressure P e  different from P c  and does not exhibit slow exponential decay, the detected defect is likely to be hydraulically well connected to another formation zone. To confirm this, a repeat detection test should be performed as described below to rule out the case of very tight cement around the probe and the detected defect. 
     To evaluate a strong communication of the defect to another zone, the probe isolation valve  117  is CLOSED after a first test. The pretest isolation valve  150  and equalizing valve  160  are OPEN to increase the pressure in the flowlines to P t . It is preferable to open the flowline isolation valve  140  to have an increased volume within the tool. Subsequently, the equalizing valve  160  is put into CLOSE position and the probe isolation valve  117  is set to OPEN position. If the new equilibrated pressure P e  is the same as it was after the first test, and the decline is to a pressure different from P c , the detected defect provides hydraulic connection to a permeable formation zone and the measured P e  is related to the formation pressure at that zone (corrected by hydrostatic gradient). 
     In a third procedure, the probe isolation valve  117  and pretest isolation valve  150  are set OPEN after the first test. The piston  175  is used to drawdown fluid from the detected defect into the pretest chamber  170 . After the drawdown is complete, the pressure is monitored by pressure gauges  120  and  130 . If the pressure quickly recovers to the same value P e  as it was after the first detection test, the detected defect is hydraulically connected to a permeable formation zone. The same procedure could also be conducted by elevating the probe pressure by moving the pretest piston forward by a small amount so that the pressure elevation is limited. 
     The sensitivity of the defect detection technique is highly dependent on the volume of the fluid in the tool flowlines and the defect volume as will be obvious in the next subsection. Therefore, in one embodiment, the pretest isolation valve  150  is in the CLOSED position thus reducing the volume of the fluid inside the tool that will be exposed to the cement annulus during drilling. 
     In one method, during drilling, the probe isolation valve  117  is in open position. With a slow drill-bit progression into the cemented annulus, an estimate of the inner radial position of the isolated defect is possible. 
     In another method, valve  117  is closed during drilling. The drill-bit penetrates through the casing and stopped at a certain position within the cemented annulus. After the fluid inside the tool is pressurized, valve  117  is open and the defect detection procedure is performed as described above. 
     Quantification (Volume Evaluation) of the Isolation Defect 
     Even if the detected defect (e.g., micro-annulus, crack or cavity) is found not to communicate to a permeable formation zone, it is useful to know the volume of the defect. The volume estimate is a key input for the remedial action plan such as a squeeze of an isolating material. In this section, we disclose the testing procedure and the interpretation to estimate the volume of the detected defect. We first introduce the following notations: 
     V t : volume of the flow-line in the tool in direct hydraulic communication with the probe 
     ρ t : density of the fluid inside the tool flowline in direct hydraulic communication with the probe 
     V d : volume of the detected defect in the cemented annulus 
     ρ d : density of the fluid occupying the detected defect in the cemented annulus, prior to drilling 
     ρ e : final density of the fluid in the combined tool and cavity system 
     c: compressibility of the fluid, assumed same within the tool and the defect 
     The mass of the fluid inside the tool before the start of the test is ρ t V t . Similarly, the mass of the fluid originally occupying the detected defect (micro-annulus) is ρ d V d . The total mass of the fluid in the tool and micro-annulus should be equal to the sum of the individual mass contributions (here we neglect a mass loss due to the flow through the cement since the pressure equilibration happens almost immediately). Therefore, mass conservation implies
 
ρ t   V   t +ρ d   V   d =ρ e ( V   t   +V   d ).  (1)
 
Using the reference state of the fluid denoted by a subscript 0 for density ρ and pressure P, we can rewrite Eq. 1
 
 V   t ρ 0   e   c(P     t     −P     0     )   +V   d ρ 0   e   c(P     c     −P     0     ) =( V   t   +V   d )ρ 0   e   c(P     e     −P     0     ) .  (2)
 
Therefore,
 
 V   t   e   cP     t     +V   d   e   cP     c   =( V   t   +V   d ) e   cP     e   .  (3)
 
Solving Eq. 3 for V d  leads to
 
     
       
         
           
             
               
                 
                   
                     V 
                     d 
                   
                   = 
                   
                     
                       V 
                       t 
                     
                     ⁢ 
                     
                       
                         
                           
                             ⅇ 
                             
                               cP 
                               t 
                             
                           
                           - 
                           
                             ⅇ 
                             
                               cP 
                               e 
                             
                           
                         
                         
                           
                             ⅇ 
                             
                               cP 
                               e 
                             
                           
                           - 
                           
                             ⅇ 
                             
                               cP 
                               e 
                             
                           
                         
                       
                       . 
                     
                   
                 
               
               
                 
                   ( 
                   4 
                   ) 
                 
               
             
           
         
       
     
     For typical values of compressibility (10 −10  Pa −1 ) and pressures (10 7  Pa), we can use first-order Taylor expansion for the exponentials in Eq. 4, which after simplification gives the final expression 
                     V   d     ≈       V   t     ⁢           P   t     -     P   e           P   e     -     P   c         .               (   5   )               
Eq. 5 shows that the sensitivity of the detection technique (i.e., the ability to detect small volume defects) depends on the volume of the tool flowlines in direct hydraulic communication with the probe, and the error associated with the measurement of pressures and V t . For maximal sensitivity, one would prefer a tool volume comparable to the size of the defect. Therefore, if the small size defects are of interest, the pretest isolation valve  150  should be CLOSED during the testing procedure to minimize the V t . Conversely, if a large volume defect is anticipated, then either the pretest chamber may be kept in a fully retracted position, by moving piston  175 , or further yet the isolation valve  140  opened to communicate to the flowline bus. Ultrasonic logs are useful in estimating the areal coverage of the defect. This is explained further below.
 
     We will also consider the case when the compressibilities of the two fluids are substantially different. This occurs when the detected defect is filled with gas. We consider the case where the fluid occupying the defect and the flowline/cement pore fluid are immiscible. In one embodiment, since P t &gt;P c , once the drill-bit penetrates into the defect, with the probe isolation valve  117  OPEN, there will be an increase in volume for the fluid in the tool flowlines and the decrease in volume for the fluid occupying the defect. 
     Let ΔV denote a change in volume in the fluid within the tool. A corresponding decrease occurs in the fluid within the defect. We start with the conservation of mass for each fluid individually.
 
ρ t   V   t =ρ te ( V   t   +ΔV )  (6)
 
and
 
ρ d   V   d =ρ de ( V   d   −ΔV ),  (7)
 
where ρ te  and ρ de  are density of the original fluid inside the tool flowline and the original fluid occupying the defect respectively under the equilibrated pressure P e . We can solve Eq. 6 so that
 
                     Δ   ⁢           ⁢   V     =         V   t     ⁡     (         ρ   t       ρ   te       -   1     )       =         V   t     ⁡     (           ρ   0     ⁢     ⅇ       c   t     ⁡     (       P   t     -     P   0       )               ρ   0     ⁢     ⅇ       c   t     ⁡     (       P   te     -     P   0       )             -   1     )       .               (   8   )               
Using first-order Taylor expansion the above equation simplifies to
 
 ΔV≈V   t   c   t ( P   t   −P   e ).  (9)
 
Solving Eq. 7 for V d  we obtain
 
     
       
         
           
             
               
                 
                   
                     V 
                     d 
                   
                   = 
                   
                     
                       Δ 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       V 
                       ⁢ 
                       
                         
                           ρ 
                           de 
                         
                         
                           
                             ρ 
                             de 
                           
                           - 
                           
                             ρ 
                             d 
                           
                         
                       
                     
                     = 
                     
                       
                         
                           Δ 
                           ⁢ 
                           
                               
                           
                           ⁢ 
                           V 
                         
                         
                           1 
                           - 
                           
                             
                               ρ 
                               d 
                             
                             / 
                             
                               ρ 
                               de 
                             
                           
                         
                       
                       . 
                     
                   
                 
               
               
                 
                   ( 
                   10 
                   ) 
                 
               
             
           
         
       
     
     The ratio ρ d /ρ de  can be expressed via compressibility and the density ρ 0  at the reference state with pressure P 0 : 
                       ρ   d       ρ   de       =           ρ   0     ⁢     ⅇ       c   d     ⁡     (       P   c     -     P   0       )               ρ   0     ⁢     ⅇ       c   d     ⁡     (       P   e     -     P   0       )             =       ⅇ       c   d     ⁡     (       P   c     -     P   e       )         .               (   11   )               
Here we have assumed that within the pressure range of interest, an average value of c d  may be used. For large ranges of pressure, one has to use an average value for compressibility relevant to the pressure difference of interest. Substituting Eq. 11 and Eq. 9 into Eq. 10 we obtain
 
                     V   d     =       V   t     ⁢           c   t     ⁡     (       P   t     -     P   e       )         1   -     ⅇ       c   d     ⁡     (       P   c     -     P   e       )             .               (   12   )               
Note that when c t =c d , Eq. 12 reduces to Eq. 5. Typical values of compressibility for gases (e.g., methane) are 100 to 1000 higher than compressibility of the liquids (e.g., water) under reservoir pressure and temperature. If the isolation defect is originally filled with gas, the final pressure is close to P c . Then, for a fixed resolution in pressure, the ability to discern the size of the defect diminishes.
 
     Advantageously, a repeat test can be performed to obtain a second estimate of V d . In one embodiment, the probe isolation valve  117  is closed and the fluid in the flowlines is pressurized as described above. Once the desired pressure P t  is reached in the tool flowlines, the valve  117  is opened and the new equilibrated pressure P e  is observed. The volume of the defect is calculated using Eq. 5 or Eq. 12 (depending on the fluid occupying the detected defect) with appropriate values of P t , P e , and P c . 
     In another embodiment, the valve  117  is opened before the repeat test is performed. With pretest isolation valve  150  closed, the fluid in the flowlines connecting valve  150  to the pretest chamber and the equalizing valve  160  is pressurized to a desired pressure P t . Once the valve  150  is open, the new equilibrated pressure P e  is observed. The volume of the detected defect is then calculated using Eq. 5 or Eq. 12 (depending on the fluid occupying the detected defect) with appropriate values of P t , P e , and P c . Note that V t  in this case will include only the volume of flowlines below valve  150  (see  FIG. 1 ). To obtain the volume of the detected defect, calculated V d  should be corrected for the volume of tool flowlines connecting valve  150  to the probe. 
     Procedure for a Gas-Filled Defect 
     For a gas-filled defect, for a change in pressure indicative of V d , we need V t c t ≈V d c d . Given that the c d /c t  ratio is about 100-1000, V t  has to be at least about 100V d . However, this is not known a priori. 
     When V t c t &lt;&lt;V d c d , P c  will drop close to P c , the initial fluid pressure within the cement. A slow transient follows this drop. Such an observation has two possibilities: (i) gas fills the defect or (ii) a perfect communication is present from the defect to the formation. A repeat experiment with a larger volume of V t , as discussed previously will allow us to judge which of the options is likely. 
     In one embodiment, the repeat experiment entails shutting valve  117  and opening equalizing valve  160 , opening flow line valve  140 , allowing the pressure to move back to P t , shutting valve  160 , and opening valve  117 . If the gas composition is known from circumstantial information, a cross-check may be carried out. Since c d  will be known for downhole conditions, knowing V t  allows us to determine V d  via Eq. 12 twice with two different values of V t . 
     Additionally, if further penetration of the probe shows that the transient to P c  is rapid, the drop in pressure is due to perfect communication between the defect and the formation. 
     Testing Procedure 
     In one embodiment, the testing procedure includes the following steps to evaluate cement integrity (see  FIG. 3 ):
         The depth of the test is selected (e.g., based on the acoustic/ultrasonic measurements such as cement bond log) at Step  305 .   Cement thickness and casing thickness are identified at Step  310  based on well completion specifications and other available information such as third interface echoes from ultrasonic measurements.   The seal around the housing with the probe is set and tested for hydraulic isolation at Step  315 .   The drill bit penetrates through the casing to a desired depth of penetration into the cemented annulus at Step  320 .   With the hydraulically isolated probe set at Step  325 , the fluid in the tool flowlines is pressurized to pressure P t &gt;P c  either by opening equalizing valve  160  or by raising the pressure in the pretest chamber  170  by moving the piston  175 .   If the pressure drop from P t  to P e  is observed at Step  330 , the drill-bit intersected the defect in the cemented annulus. The position of the drill bit at the time of the pressure drop will indicate the position of the isolation defect. If no pressure drop is observed, proceed to Step  350  to estimate cement permeability following procedures disclosed in U.S. Pat. No. 7,753,118.   Repeat the pressure test as described in embodiments above to determining if the detected defect is directly connected to a permeable formation zone (Step  335 ).   If the detected defect is proved to be not connected to a formation at Step  340 , proceed to Step  345  and use the data from the two pressure tests (Steps  325  and  335 ) to estimate the volume of the detected defect using Eq. 5 or Eq. 12 (depending on the fluids filling the defect and the tool flowline). Repeat the test to obtain additional estimate of the volume, if necessary.   Proceed to Step  350  to evaluate the permeability of the cement around the probe and the detected isolation defect by using interpretation technique as described in U.S. Pat. No. 7,753,118, but suitably corrected by accounting for the presence of the defect. Specifically, the boundary value problem has to be solved with a penetrating probe intersecting a slit, and thus a third parameter (L/r p ) is necessary, the other two being L p /r p , and L c /r p , where L p  is the penetration distance of the probe into the cement, and L c  is the cement thickness. A geometrical assumption with regard to the shape of the defect from sonic logs and the volume of the defect is needed. An example of this is shown below and is illustrated in  FIG. 4 .   If the detected defect is proved to be connected to a permeable formation zone at Step  340 , zonal isolation at the depth of test is compromised. Proceed to Step  360  and start remedial action planning.       

     Transmissibility Estimate 
     Remedial action to restore cement integrity might include squeezing sealing material into the detected defect. The transmissibility of the defect is an important property to evaluate before the remedial job is performed. The transmissibility of the defect is a measure of the defect&#39;s ability to facilitate longitudinal flow, meaning flow along the annulus or a gap caused by the defect. As a practical matter, if the defect is directly connected to the permeable formation zone no effective estimate of its volume using the disclosed procedure is available. The effective transmissibility of the micro-annulus that is not directly connected to the formation zone may be estimated as follows. 
       FIG. 4   a  shows a schematic representation of the cross-sectional (top) view of the wellbore-casing-annulus system. Casing  420  isolates wellbore  410  from formation  450 . The annulus between casing  420  and formation  450  is filled with cement  430 . The micro-annulus  440  and other isolation defects might be present in the cement annulus  430 . 
     Let us, for example, consider a patch of area A (see  FIG. 4   b ) where a micro-annulus  440  is detected next to the casing  420 . If the micro-annulus  440  is thin enough, since the area is on a cylindrical surface, the width of the gap is 
                   b   =         V   d     A     .             (   13   )               
Let the length of the defect along the borehole be L (as shown in  FIG. 4   b ). The average width of the defect is
 
 W=A/L.   (14)
 
     By solving standard Stokes flow in this slit, and assuming a uniform average width W, we have the following expression for flow rate through the isolation defect when a pressure difference of ΔP exists across L 
                     Q   =       2     3   ⁢   μ       ⁢       Δ   ⁢           ⁢   P     L     ⁢       b   3     8     ⁢   W       ,           (   15   )               
where μ is the shear coefficient of viscosity. Thus, fluid loss through the defect in a co-mingled system may be calculated.
 
     Based on the cement ultrasonic logs, it may be desirable to know the extent of hydraulic isolation, or more appropriately lack of it. In many instances such a test is desirable before the casing is perforated. Once perforated, a defect may connect two separate zones. For such cases, the above expression is useful to know the extent of potential communication. If upon estimate of the volume, it is suggested that the width W is small, hydraulic communication may be sufficiently small that a remedy may not be necessary. Additionally, two separate tests revealing quite different defect volumes when set at two different positions also indicate that the defect seen on a ultrasonic tool comprises separate defects that appear overlapping. The images obtained by sonic or ultrasonic tools contain various levels of processing that may introduce occasional artifacts not resolvable in the absence of additional data. Thus, in the context of  FIG. 4   a  and  FIG. 4   b , what appears as an indication of a single defect in an ultrasonic log is resolved to be fully connected of not through the above disclosed procedure for volume estimation. 
     For estimating the cement permeability around the probe and the detected defect the boundary value problem has to be solved with a penetrating probe intersecting a slit. In order to account for a complex geometry of a probe-defect-annulus system a third parameter (L/r p ) is necessary, the other two being L p /r p , and L/r p , where L p  is the penetration distance of the probe into the cement, and L c  is the cement thickness. Relationships for the correction factor as illustrated in the prior patents (U.S. Pat. No. 7,753,118) are necessary. 
     In another embodiment, one can measure the transmissibility of the detected defect directly by squeezing in the fluid with known PVT properties from the pretest chamber and measuring the change in pressure with gauges  120  and  130 , and inferring the flow rate via change in the position of the piston  175  inside the pretest chamber  170 . Advantageously, this method can be also applied in the case when the detected defect is found to be in direct hydraulic communication with permeable formation zone. 
     Although only a few example embodiments have been described in detail above, those skilled in the art will readily appreciate that many modifications are possible in the example embodiments without materially departing from this invention. Accordingly, all such modifications are intended to be included within the scope of this disclosure as defined in the following claims. In the claims, means-plus-function clauses are intended to cover the structures described herein as performing the recited function and not only structural equivalents, but also equivalent structures. Thus, although a nail and a screw may not be structural equivalents in that a nail employs a cylindrical surface to secure wooden parts together, whereas a screw employs a helical surface, in the environment of fastening wooden parts, a nail and a screw may be equivalent structures. It is the express intention of the applicant not to invoke 35 U.S.C. §112, paragraph 6 for any limitations of any of the claims herein, except for those in which the claim expressly uses the words ‘means for’ together with an associated function.