Page 359 - Standard Handbook Petroleum Natural Gas Engineering VOLUME2
P. 359

346   Reservoir Engineering


                                            Thermal Recovery
                   In-Sltu Combustion

                     The  theory  and  practice  of  in-situ combustion  or fireflooding is  covered
                   comprehensively in  the  recent  SPE  monograph on  thermal recovery by  Prats
                   [378]. In addition, the continuing evolution of screening criteria for fireflooding
                   [398,399] and steamflooding [400] have been reviewed and evaluated by  Chu.
                   A  recent appraisal of in-situ combustion was provided by  White  [401] and the
                   status of oxygen fireflooding was provided by  Garon  [402].
                     Part of  the appeal of fireflooding comes from the fact that it uses the world’s
                   cheapest and most  plentiful fluids  for  injection: air  and water.  However,  sig-
                   nificant amounts of  fuel must be burned, both above the  ground to  compress
                   the air, and below ground in the combustion process. Fortunately, the worst part
                   of  the  crude oil is burned; the lighter ends are carried forward in advance of
                   the burning zone to upgrade the  crude oil.


                   Steam Flooding
                     Of  all  of  the  enhanced oil  recovery processes currently available, only  the
                   steam drive  (steamflooding) process is  routinely used  on  a  commercial basis.
                   In  the  United  States, a  majority  of  the  field  testing with  this  process  has
                   occurred in California, where many of  the shallow, high-oil-saturation reservoirs
                   are good candidates for thermal recovery. These reservoirs contain high-viscosity
                   crude oils that are difficult to mobilize by  methods other than thermal recovery.
                     In  the  steam drive process,  steam is  continuously introduced into injection
                   wells  to  reduce the viscosity of  heavy  oil and provide a driving force to move
                   the more mobile oil towards the producing wells. In typical steam drive projects,
                   the injected fluid at the  surface may  contain about 80% steam and 20% water
                   (80% quality) [380]. When steam is injected into the reservoir, heat is transferred
                   to the oil-bearing formation, the reservoir fluids, and some of  the adjacent cap
                   and base rock. As  a result, some of  the steam condenses to yield a mixture of
                   steam and hot water flowing through the  reservoir.
                     The steam drive may  work by  driving the water and oil to form an oil bank
                   ahead of  the steamed zone. Ideally this oil bank remains in front, increasing in
                   size until it is produced by  the wells  offsetting the injector. However, in many
                   cases, the steam flows over the oil and transfers heat to the oil by  conduction.
                   Oil at the interface is lowered in viscosity and dragged along with the steam to
                   the producing wells. Recoverability is increased because the steam (heat) lowers
                   the oil viscosity and improves oil mobility. As  the more mobile oil is displaced
                   the  steam zone  expands vertically, and  the  steam-oil interface is  maintained.
                   This process is energy-intensive since it requires the use of a significant fraction
                   (25%-40%)  of  the energy in the produced petroleum for the generation of  steam.
                     In steamflooding, the rate of  steam injection is initially high to minimize heat
                   losses to the cap and base rock. Because of reservoir heterogeneities and gravity
                   segregation of  the condensed water from the steam vapor, a highly permeable
                   and  relatively oil-free channel often  develops between  injector  and producer.
                   Many  times this channel occurs near the top of  the oil-bearing rock, and much
                   of the injected heat is conducted to the caprock as heat loss rather than being
                   conducted to oil-bearing sand where the heat is needed. In addition, the steam
                   cannot displace oil efficiently since little oil is left in the channel. Consequently,
                   neither  the  gas  drive from  the  steam vapor nor  the  convective heat  transfer
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