Page 86 - Hydrocarbon
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Drilling Engineering                                                   73


                                Surface

                                  Conductor/
                                   stovepipe

                                      Surface
                                       casing

                                     Intermediate
                                         casing


                                        Production
                                           casing

                                         Production
                                              liner
             Figure 4.24 Casing scheme.


             with the hole collapsing around the drill bit, with the loss of drilling fluid into
             formations with low pressure or in the worst case with the uncontrolled flow of gas
             or oil from the reservoir into unprotected shallow formations or to the surface
             (blowout). Hence, from time to time, the borehole needs to be stabilised and the
             drilling progress safeguarded.
                                                                            5
                The casing design will usually start with a 23 in. conductor, then 18 in. surface
                                                                            8
                      3
                                                            5
             casing, 13 in. intermediate casing above reservoir, 9 in. production casing across
                      8                                     8
             reservoir section and possibly 7 in. production ‘liner’ over a deeper reservoir section
             (Figure 4.24). A liner is a casing string which is clamped with a packer into the
             bottom part of the previous casing; it does not extend all the way to the surface, and
             thus saves cost.
                Casing joints are available in different grades, depending on the expected loads
             to which the string will be exposed during running, and the lifetime of the well.
             The main criteria for casing selection are

               Collapse load: originates from the hydrostatic pressure of drilling fluid, cement
                slurry outside the casing and later on by ‘moving formations’, for example salt
               Burst load: this is the internal pressure the casing will be exposed to during
                operations
               Tension load: caused by the string weight during running in; it will be highest at
                the top joints
               Corrosion service: carbon dioxide (CO 2 ) or hydrogen sulphide (H 2 S) in formation
                fluids will cause rapid corrosion of standard carbon steel and therefore special steel
                may be required
               Buckling resistance: the load exerted on the casing if under compression.

             The casing will also carry the BOPs described earlier.
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