Abstract:
A method for continuously mixing a borehole fluid such as cement includes using a measurement of the solid fraction of a cement slurry as it is being mixed to determine the ratio of the solid and liquid components to be added to the slurry. A system for mixing the includes a liquid material (water) supply including a flow meter; a solid material (cement) supply; a mixer which receives the liquid and solid materials and includes an output for delivering materials from the mixer to a delivery system; a device for measuring the amount of material in the mixer; and a flow meter in the output; wherein measurements from the flow meters and the device for measuring the amount of material in the mixer are used to control the amount of solid and/or liquid material added to the mixer.

Description:
FIELD OF THE INVENTION  
         [0001]    The present invention relates to a system for mixing fluids containing solid and liquid materials such as cement. In particular the invention provides a system for the continuous mixing of cements or other fluids used in the drilling, completion or stimulation of boreholes such as oil or gas wells.  
         BACKGROUND OF THE INVENTION  
         [0002]    When a well such as an oil or gas well has been drilled, it is often desired to isolate the various producing zones form each other or from the well itself in order to stabilise the well or prevent fluid communication between the zones or shut off unwanted fluid production such as water. This isolation is typically achieved by installing a tubular casing in the well and filling the annulus between the outside of the casing and the wall of the well (the formation) with cement. The cement is usually placed in the annulus by pumping a slurry of the cement down the casing such that it exits at the bottom of the well and passes back up the outside of the casing to fill the annulus. While it is possible to mix the cement as a batch prior to pumping into the well, it has become desirable to effect continuous mixing of the cement slurry at the surface just prior to pumping into the well. This has been found to provide better control of cement properties and more efficient use of materials.  
           [0003]    The cement slurries used in such operations comprise a mixture of dry and liquid materials. The liquid phase is typically water and so is readily available and cheap. The solid materials define the slurry and cement properties when added to the water and mixed, the amount of solid materials in the slurry being important. Since the liquid phase is constant, the amount of solid material added is usually monitored by measuring the density of the slurry and maintaining this at the desired level by controlling the amount of the solid material being added. FIG. 1 shows a schematic diagram of a prior art mixing system. In the system of FIG. 1, mix water is pumped from a feed supply  10  via a pump  12  to a mixer  14  which feeds into a mixing tub  16 . Solid materials are delivered to the mixer  14  from a surge can  18  via a flow control valve  20  and are carried into the mixing tub  16  with the mix water. The contents of the mixing tub  16  are recirculated through a recirculation pipe  22  and pump  24  to the mixer  14 . The recirculation pipe  22  also includes a densitometer  26  which provides a measurement of the density of the slurry in the mixing tub  16 . An output  28  is provided for slurry to be fed from the mixing tub  16  to further pumps (not shown) for pumping into the well. Control of the slurry mixture is achieved by controlling the density in the mixing tub  16  as provided by the densitometer  26  by addition of solid material so stay at a predetermined level for the slurry desired to be pumped. The densitometer  26  is typically a non-radioactive device such as a Coriolis meter.  
           [0004]    While this system is effective for slurries using materials of much higher density than water, it is not effective for slurries using low density solid materials, especially when the density of the solids is close to that of water. In such cases, a density measurement is not sensitive enough to control the amounts of solid material added to the necessary accuracy.  
           [0005]    The present invention seeks to provide a mixing system which avoid the problem of density measurement described above.  
         SUMMARY OF THE INVENTION  
         [0006]    In its broadest aspect, the present invention comprises using a measurement of the solid fraction of a fluid as it is being mixed to determine the ratio of the solid and liquid components added to the slurry.  
           [0007]    The invention is particularly applicable to the mixing of borehole cement slurries, in which case, solids fraction is determined as (slurry vol−water vol)/slurry vol. An alternative but related parameter is porosity, determined as water vol/slurry vol (porosity+solids fraction=1).  
           [0008]    A system for mixing cement in accordance with the invention comprises a water supply including a flow meter; a solid material supply; a mixer which receives the water and solid materials and includes an output for delivering materials from the mixer to a delivery system; a device for measuring the amount of material in the mixer; and a flow meter in the output; wherein measurements from the flow meters and the device for measuring the amount of material in the mixer are used to control the amount of solid material added to the mixer.  
           [0009]    The flow meters can be mass flow meters or volumetric flow meters. Any suitable form of meter can be used, for example Coriolis meters or electromagnetic meters.  
           [0010]    The mixer will typically include a tank or tub, in which case the device for measuring the amount of material in the mixer can be a level sensor. Such a level sensor is preferably a time domain reflectometry- or radar-type device although acoustic or float devices can also be used. It is preferred to mount such a device in an arrangement for damping transient fluctuations in the tank level, for example in an arrangement of concentric slotted tubes. An alternative or additional form of sensor can be a load cell which can be used to indicate the weight of the tank, or a pressure sensor.  
           [0011]    Where the mixer includes some form of recirculation of the slurry through the tank, it is important that the output flow meter is downstream of this recirculation.  
           [0012]    Where the solid materials comprise cement and other solid additives added separately to the mixer, separate flow meters can also be provided for each separate supply of additives.  
           [0013]    In its simplest form, the measurement of solid fraction is used as a guide for the operator to add solids, particularly cement, to the slurry as it is mixed. In more advanced versions, the calculation of solids fraction is used to control the addition of solids directly by means of an automatic control system. 
       
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS  
       [0014]    [0014]FIG. 1 shows a prior art mixing system;  
         [0015]    [0015]FIG. 2 shows a mixing system according to a first embodiment of the invention;  
         [0016]    [0016]FIG. 3 shows the components of a tank level sensor;  
         [0017]    [0017]FIG. 4 shows the components of the level sensor assembled;  
         [0018]    [0018]FIG. 5 shows a schematic of the tank level measurement; and  
         [0019]    [0019]FIG. 6 shows a mixing system according to a second embodiment of the invention. 
     
    
     DESCRIPTION OF THE PREFERRED EMBODIMENT  
       [0020]    The system shown in FIG. 2 is used for the continuous mixing of cement for oil well cementing operations and comprises a supply of mix water  100  feeding, via a pump  102  and a flow meter  104  to a mixing system  106 . The mixing system  106  also receives solid materials from a surge can  108  which are admitted through a valve  110 . The mixed solid and liquid materials are delivered through a feed pipe  112  to a mixing tub  114 . The mixing tub  114  has a first outlet  116  connected to a recirculation pump  118  which feeds the slurry drawn from the tub  114  back into the mixing system. The tub  114  is provided with a level sensor  120  and/or a load sensor  122  to provide an indication of the tank contents and any change in contents over time. A second output  124 ′ is provided from the tub  114  which leads, via a second pump  126  and a second flow meter  128 ′ to the pumping system from which it is delivered to the well (not shown). An alternative method of delivery (shown in dashed line in FIG. 2) has an output  124 ′ taken from the recirculation line via a flow meter  128 ′ to the well. Other arrangements are also possible. The pumps  102 ,  118 ,  126  are of the usual type found in well cementing systems, for example centrifugal pumps. Likewise, the flow meters  104 ,  128 ′ are conventional, for example Coriolis meters such as those that have been used as densitometers in previous applications. Different types of pumps and meters each have advantages and disadvantages that are well known in the art and can be selected according to requirements.  
         [0021]    FIGS.  3 - 5  show details of the tub level sensor and its installation. The sensor comprises a Krohne radar sensor  200 , a stainless steel rod  202 , an inner slotted sleeve  204  and an outer slotted sleeve  206 . The rod  202  is screwed onto the sensor  200  and the inner sleeve  204  mounted over the rod  202  and attached to a flange on the sensor  200 . The outer sleeve  206  is mounted over the inner sleeve  204  to which it is attached. In use, the sensor arrangement is installed in the mixing tub  114  in the vertical position and in a location where the slurry is renewed as the mixing occurs, to avoid location in a dead zone where cement might set. The sensor provides a measurement of the difference between the length of the rod  202  (LM) and the level of slurry in the tub level (TL). The free tub level (FTL) is obtained by:  
         
       FTL=LM−TL.  
     
         [0022]    It will be appreciated that the exact form of level sensor is not important to the overall effect of the invention. What is important is to obtain an indication of the variation versus time of the tub slurry volume (called “tub flow” in this document). This can be obtained using a float or a load sensor or combinations of any of these or any other sensor giving this information.  
         [0023]    The outputs of the flow sensors and level sensors are used to monitor the solid fraction of the slurry in the following manner:  
         [0024]    The solid fraction computation is based on the balance between incoming and outgoing volumes (or flow rates) as expressed in the following relationship:  
         
       Q 
       water 
       +Q 
       cement 
       =Q 
       slurry 
       +Q 
       tub  
     
         [0025]    where Q tub  is the tub rate.  
         [0026]    Tub rate is the variation versus time of the tub volume and is considered as positive while the tub level increases and negative while it decreases. The smaller the tub cross section, the more sensitive the measurement will be to change. Q tub  is given by:  
         Q   tub     =       S   tub                 h   tub            t                               
 
         [0027]    where S tub  is the tub cross section and  
              h   tub            t                           
 
         [0028]    is the tub level variation over time. In the simplest case, the tub section is constant and the tub rate becomes the product of the tub level variation/time and the tub cross section.  
         [0029]    The solids fraction at time t is computed as the ratio of (slurry vol−water vol) over the total slurry volume present at time t in the tub. The variation in tub slurry volume V tub (t+δt)−V tub (t) can be expressed as:  
           V   tub ( t+δt )− V   tub ( t )=[ Q   water ( t )+ Q   cement ( t )− Q   slurry ( t )]*δ t    
         [0030]    which can be rewritten as:  
           V   tub ( t+δt )− V   tub ( t )= Q   tub ( t )*δ t.    
         [0031]    In the same way, the variation in the water volume present in the tub at time t V water (t+δt)−V water (t) is equal to the incoming water volume minus the amount of water present in the slurry leaving the tub, and can be expressed as:  
           V   water ( t+δt )− V   water ( t )=[ Q   water ( t )−(1−SolidFraction( t ))* Q   slurry ( t )]*δ t.    
         [0032]    Solid Fraction is then expressed as:  
         SolidFraction        (     t   +     δ                 t       )       =     1   -           V   water          (   t   )       +       [         Q   water          (   t   )       -       (     1   -     SolidFraction        (   t   )         )     *       Q   slurry          (   t   )           ]     *   δ                 t             V   tub          (   t   )       +         Q                tub            (   t   )       *   δ                 t                                 
 
         [0033]    The calculation requires that the initial conditions be known if it is to be accurate ab initio, i.e. is the tub empty, full of water or containing slurry already. The calculation will ultimately stabilise independently of the initial conditions, the time taken to do this depending on the tub volume and the output flow rate Q slurry .  
         [0034]    These calculations are conveniently performed using a computer, in which case the measurements can be provided directly from the sensors via a suitable interface. A preferred screen display will show the various flow rates or levels, together with the desired solids fraction (calculated when designing the slurry). The mixing process is controlled by adjusting the amount of cement and/or water added to the mixer so as to maintain the calculated solids fraction at the desired level. Alternatively, the results of the calculations can be fed to an automatic control system which adjusts the rate at which the components are delivered to the mixing system.  
         [0035]    The system described above works well when the dry ingredients (blend of cement+additives) are delivered pre-mixed to the well site from another location. In this case essentially the same measurements and calculations as described above are performed, merely substituting Q blend  for Q cement . If it is desired to mix the dry materials on site as part of the continuous mixing process, a slightly different approach is required. FIG. 6 shows a mixing system according to another embodiment of the invention and uses a numbering scheme which follows that of FIG. 2. The system of FIG. 6 comprises an additional dry material supply  130  which admits the dry products to the mixing system  106  via a mass flow meter  132  (other flow measurement means can also be used) and a control valve  134 . In this case, the basic control equation becomes:  
         
       Q 
       water 
       +Q 
       additive 
       +Q 
       cement 
       =Q 
       tub 
       +Q 
       slurry  
     
         [0036]    where four of the five variables are know and Q cement  is the most difficult parameter to measure accurately. Where multiple dry additives are to be added, the supply can comprise separate material supplies, each with a flow meter and valve. Additional terms Q additive1 , Q additive2 , etc., are included in the control equation.  
         [0037]    It will be appreciated that changes can be made in implementation while still remaining within the scope of using solid fraction as the property monitored to effect control of the mixing.  
         [0038]    For example, the method can be applied to the mixing of other borehole fluids such as stimulation fluids (fracturing fluids) or even drilling fluids (mud). In the case of fracturing fluids, the gel and proppant (liquid and solid phases) are usually mixed using a pod blender and the proportion of gel and proppant controlled using a densitometer (usually radioactive) downstream of the mixer/blender. The use of radioactive sensors generates many environmental issues and while Coriolis-type meters are an alternative, they are know to have limitations in respect of flow rate when used this way. The present invention allows control of proppant and gel concentrations by means of flow meters without the need to rely on densitometer measurements.  
         [0039]    Gel and mixed fluid flow rates are measured by means of electromagnetic flow meters. The amount of proppant is directly deduced from the following relationship:  
         
       Q 
       gel 
       +Q 
       Pr oppant 
       =Q 
       MixedFluid  
     
         [0040]    Proppant concentration (in Pounds Per Gallon Added or “PPA”) can be a function of solid fraction as defined above and expressed as the following:  
           PPA =Proppant Density*Solid Fraction/(1−Solid Fraction).  
         [0041]    Thus the solid fraction measurement methodology described above in relation to cement can be applied to fracturing fluids by determining proppant density rather than cement density.  
         [0042]    This approach has the advantage of not requiring the use of radioactive densitometers thus avoiding limitations placed on use for regulatory reasons and without the flow rate performance limitations of other measurement techniques. The equipment and control system is essentially the same as that used in the cementing system described above.