Patent Publication Number: US-8968580-B2

Title: Apparatus and method for regulating flow through a pumpbox

Description:
BACKGROUND OF THE INVENTION 
     1. Field of Invention 
     This invention relates generally to processing of a feedstock and more particularly to a pumpbox for receiving a hydrocarbon feedstock. 
     2. Description of Related Art 
     Hydrocarbon feedstocks are generally viscous and may be entrained with other components such as rock, sand, clay and other minerals. As a result, such feedstocks require processing to separate useful hydrocarbon products from residue before transport and refining. 
     One example of a hydrocarbon ore deposit is the Northern Alberta oil sands, which comprises about 70 to about 90 percent by weight of mineral solids including sand and clay, about 1 to about 10 percent by weight of water, and a bitumen or oil film. The bitumen may be present in amounts ranging from a trace amount up to as much as 20 percent by weight. Due to the highly viscous nature of bitumen, when excavated some of the ore may remain as clumps of oversize ore that requires sizing to produce a sized ore feed suitable for processing. The ore may also be frozen due to the northerly geographic location of many oil sands deposits, making sizing of the ore more difficult. The sized ore feed is typically processed by adding water to form a slurry in a location proximate to the ore deposit, and the resulting slurry is hydro-transported through a pipeline to a processing plant, where the slurry forms the feedstock for a processing plant that separates hydrocarbon products from the sand and other minerals. 
     Low specific gravity hydrocarbons such as bitumen froth may be separated from sand and water, which generally have higher specific gravity, by various gravity separation processes. There remains a need for improved processes and apparatus for treating heavy hydrocarbon feedstocks. 
     SUMMARY OF THE INVENTION 
     In accordance with one aspect of the invention there is provided a pumpbox apparatus. The apparatus includes a reservoir volume having a first inlet for receiving a feedstock stream and a second inlet for receiving a water stream, the reservoir volume being in communication with a discharge outlet disposed to discharge accumulated liquid from the reservoir volume. The reservoir volume is operable to accumulate the feedstock stream and the water stream to a first liquid level in the reservoir volume while withdrawing a discharge stream through the discharge outlet to cause a flow of liquid through the pumpbox. The first inlet is located above the second inlet and defines a first flow velocity region between the first inlet and the second inlet and a second flow velocity region between the second inlet and the discharge outlet. The first flow velocity is lower than the second flow velocity to facilitate flotation of a low specific gravity portion of the feedstock through the first region toward an upper surface of the liquid accumulated in the reservoir volume. The apparatus also includes a collector for collecting at least a portion of the low specific gravity portion from an upper surface of the accumulated volume when the first liquid level is above the first inlet. 
     The apparatus may include a controller for controlling a flow rate through the discharge outlet to maintain the first liquid level at a level between the first inlet and a high liquid level, the high liquid level being a desired maximum operating level for the reservoir volume. 
     The collector may be operably configured to collect at least a portion of the low specific gravity portion from an upper surface of the accumulated volume when the first liquid level reaches a high liquid level. 
     The collector may include a launder having an inlet disposed in the reservoir volume at the high liquid level for receiving an overflow of the low specific gravity portion from the reservoir volume. 
     The reservoir volume may be selected to maintain a retention time of feedstock and water in the pumpbox in the range of about 30 seconds to about several minutes at an expected average flow rate of the feedstock stream and the water stream. In one arrangement, the retention time is about 1 minute. 
     The apparatus may include a discharge pump in communication with the discharge outlet for withdrawing the discharge stream from the discharge outlet. 
     The discharge pump may be operably configured to discontinue operation when the liquid level reaches a low liquid level. 
     The apparatus may include a controller operably configured to control operation of the discharge pump in response to receiving a liquid level signal representing an accumulation level of liquid in the reservoir volume. 
     The feedstock stream may include bitumen. In one embodiment, the feedstock stream comprises bitumen froth. In another embodiment, the bitumen froth is in the form of an aerated froth. In another variation, the feedstock stream comprises bitumen froth in the form of a highly aerated bitumen froth. Highly aerated bitumen froths tend to float fast. Advantageously, in one aspect of the invention, the vessel is operative to selectively separate out such a fast floating aerated bitumen froth. 
     The feedstock stream may include water and solids. 
     The water stream may include a re-circulated water stream. 
     The re-circulated water stream may include residual bitumen and solids. 
     The second inlet may be disposed to cause solids that settle out of the accumulated liquid volume to be dispersed toward the discharge outlet for discharge in the discharge stream. 
     The second inlet may be oriented to direct the water stream received at the second inlet generally towards the discharge outlet. 
     The pumpbox may include a base having portion that may be inclined to direct solids that settle out of the accumulated liquid volume toward the discharge outlet for discharge in the discharge stream. 
     A density of the discharge stream may be between about 122×10 1  and about 128×10 1  kg/m3. 
     The flow velocity in the first flow velocity region may be less than about 5×10 −2  meters per second. 
     In accordance with another aspect of the invention there is provided a pumpbox apparatus. The apparatus includes a reservoir volume having a first inlet for receiving a feedstock stream and a second inlet for receiving a water stream, the reservoir volume being in communication with a discharge outlet disposed to discharge accumulated liquid from the reservoir volume. The reservoir volume is operable to accumulate the feedstock stream and the water stream to a first liquid level in the reservoir volume while withdrawing a discharge stream through the discharge outlet to cause a flow of liquid through the pumpbox. The first inlet is located above the second inlet and defines a first flow velocity region between the first inlet and the second inlet and a second flow velocity region between the second inlet and the discharge outlet, the first flow velocity being lower than the second flow velocity to facilitate flotation of a low specific gravity portion of the feedstock through the first region toward an upper surface of the liquid accumulated in the reservoir volume. The apparatus also includes provisions for collecting at least a portion of the low specific gravity portion from an upper surface of the accumulated volume when the first liquid level is above the first inlet. 
     The apparatus may include provisions for controlling a flow rate through the discharge outlet to maintain the first liquid level at a level between the first inlet and a high liquid level, the high liquid level being a desired maximum operating level for the pumpbox. 
     The provisions for collecting may include provisions for collecting at least a portion of the low specific gravity portion from an upper surface of the accumulated volume when the first liquid level reaches a high liquid level. 
     The provisions for controlling may include provisions for controlling a flow rate through the discharge outlet to maintain a retention time of the feedstock stream and water stream in the reservoir volume of about 1 minute. 
     The apparatus may include provisions for causing solids that settle out of the accumulated liquid volume to be dispersed toward the discharge outlet for discharge in the discharge stream. 
     A density of the discharge stream may be between about 122×10 1  and about 128×10 1  kg/m3. 
     The flow velocity in the first flow velocity region may be less than about 5×10 −2  meters per second. 
     In accordance with another aspect of the invention there is provided a method for regulating flow through a pumpbox having a reservoir volume in communication with a discharge outlet disposed to discharge accumulated liquid from the reservoir volume. The method involves receiving a feedstock stream at a first inlet of the reservoir volume, receiving a water stream at a second inlet of the reservoir volume, and accumulating the feedstock stream and the water stream to a first liquid level in the reservoir volume while withdrawing a discharge stream through the discharge outlet to cause a flow of liquid through the pumpbox. The first inlet is located above the second inlet and defines a first flow velocity region between the first inlet and the second inlet and a second flow velocity region between the second inlet and the discharge outlet, the first flow velocity being lower than the second flow velocity to facilitate flotation of a low specific gravity portion of the feedstock through the first region toward an upper surface of the liquid accumulated in the reservoir volume. The method further involves collecting at least a portion of the low specific gravity portion from an upper surface of the accumulated volume when the first liquid level is above the first inlet. 
     The method may involve controlling a flow rate through the discharge outlet to maintain the first liquid level at a level between the first inlet and a high liquid level, the high liquid level being a desired maximum operating level for the reservoir volume. 
     Collecting may involve collecting at least a portion of the low specific gravity portion from an upper surface of the accumulated volume when the first liquid level reaches a high liquid level. 
     Collecting may involve causing the low specific gravity portion to overflow into a launder having an inlet disposed in the reservoir volume at the high liquid level. 
     Withdrawing the discharge stream may involve operating a discharge pump in communication with the discharge outlet. 
     The method may involve discontinuing operation of the discharge pump when the liquid level reaches a low liquid level. 
     The method may involve controlling operation of the discharge pump in response to receiving a liquid level signal representing an accumulation level of liquid in the reservoir volume. 
     The method may involve causing solids that settle out of the accumulated liquid volume to be dispersed toward the discharge outlet for discharge in the discharge stream. 
     Causing solids that settle out of the accumulated liquid volume to be dispersed may involve directing the water stream received at the second inlet generally towards the discharge outlet. 
     A density of the discharge stream may be between about 122×10 1  and about 128×10 1  kg/m3. 
     The flow velocity in the first flow velocity region may be less than about 5×10 −2  meters per second. 
     In accordance with one aspect of the invention there is provided a system for extracting bitumen from a feedstock. The system includes a pumpbox including a reservoir volume having a first inlet for receiving a feedstock stream including bitumen and a second inlet for receiving a water stream. The reservoir volume is in communication with a discharge outlet disposed to discharge accumulated liquid from the reservoir volume. The reservoir volume is operable to accumulate the feedstock stream and the water stream to a first liquid level in the reservoir volume while withdrawing a discharge stream through the discharge outlet to cause a flow of liquid through the pumpbox. The first inlet is located above the second inlet and defines a first flow velocity region between the first inlet and the second inlet and a second flow velocity region between the second inlet and the discharge outlet. The first flow velocity is lower than the second flow velocity to facilitate flotation of at least a portion of the bitumen through the first region toward an upper surface of the liquid accumulated in the reservoir volume. The system also includes a first hydrocyclone having a feed inlet, an overflow discharge outlet for producing a first product stream, and an underflow discharge outlet, the feed inlet of the first hydrocyclone being in communication with the discharge outlet of the pumpbox for receiving the discharge stream from the pumpbox. The system further includes a second hydrocyclone having a feed inlet, an overflow discharge outlet, and an underflow discharge outlet for producing a first tailings stream, the feed inlet of the second hydrocyclone being in communication with the underflow discharge outlet of the first hydrocyclone. The overflow discharge outlet of the second hydrocyclone is in communication with the second inlet of the pumpbox for providing the water stream to the pumpbox. The pumpbox further includes a collector for collecting at least a portion of the low specific gravity bitumen portion from an upper surface of the accumulated volume when the first liquid level is above the first inlet to produce a second product stream, the second product stream being combined with the first product stream to produce a system product stream. 
     The system may include a third hydrocyclone having a feed inlet, an overflow discharge outlet, and an underflow discharge outlet, the feed inlet of the third hydrocyclone being in communication with the underflow discharge outlet of the second hydrocyclone for receiving the first tailings stream, the third hydrocyclone being operable to produce a second tailings stream at the underflow discharge outlet of the second hydrocyclone, the overflow discharge outlet of the third hydrocyclone being in communication with the feed inlet of the second hydrocyclone to provide an additional feed to the second hydrocyclone. 
     Other aspects and features of the present invention will become apparent to those ordinarily skilled in the art upon review of the following description of specific embodiments of the invention in conjunction with the accompanying figures. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
       In drawings which illustrate embodiments of the invention, 
         FIG. 1  is a perspective partially cut-away view of a pumpbox apparatus in accordance with a first embodiment of the invention; 
         FIG. 2  is a side schematic view of the pumpbox shown in  FIG. 2 ; and 
         FIG. 3  is a schematic flow diagram of a system for extracting bitumen employing the pumpbox shown in  FIG. 1 . 
     
    
    
     DETAILED DESCRIPTION 
     Referring to  FIG. 1 , a pumpbox apparatus according to a first embodiment of the invention is shown generally at  100 . The pumpbox apparatus  100  includes a reservoir volume  102  having a first inlet  104  for receiving a feedstock stream and a second inlet  106  for receiving a water stream. The reservoir volume  102  is in communication with a discharge outlet  108  disposed to discharge accumulated liquid from the reservoir volume. The reservoir volume  102  is operable to accumulate the feedstock stream received at the first inlet  104  and the water stream received at the second inlet  106  to a first liquid level in the reservoir volume while withdrawing a discharge stream through the discharge outlet  108  to cause a flow of liquid through the pumpbox apparatus  100 . In one embodiment the density of the discharge stream may be between about 122×10 1  and about 128×10 1  kg/m3. 
     The first inlet  104  is located above the second inlet  106 . In this embodiment the first inlet  104  is in communication with a feed conduit  105 , which is receives the feedstock stream, and directs the stream to the first inlet  104 . The pumpbox apparatus  100  is shown in side schematic view in  FIG. 2 . Referring to  FIG. 2 , the feedstock stream received at the first inlet  104  and the water stream received at the second inlet  106  cause respective flows  142  and  143  in the reservoir volume  102 . A first flow velocity region  144  is defined between the first inlet  104  and the second inlet  106 . A second flow velocity region  146  is defined generally between the second inlet  106  and the discharge outlet  108 . A first flow velocity in the first region  144  is lower than a second flow velocity in the second region  144 , which facilitates flotation of a low specific gravity portion of the feedstock through the first region  144  toward an upper surface  148  of the liquid accumulated in the reservoir volume  102 . 
     The flow through the first and second flow velocity regions  144  and  146  is generally in a downwards direction and in one embodiment where the feedstock stream comprises bitumen, the first flow velocity is less than about 5×10 −2  meters per second, which permits a fast rising bitumen portion to float upwardly in the reservoir volume  102 . Referring back to  FIG. 1 , the pumpbox apparatus  100  further includes a collector  110  for collecting at least a portion of the low specific gravity portion of the feedstock from the upper surface  148  when the first liquid level is above the first inlet  104 . 
     In the embodiment shown in  FIG. 2 , the pumpbox apparatus  100  further includes a discharge pump  160 . The discharge pump  160  includes an inlet  162  in communication with the discharge outlet  108  for withdrawing the discharge stream from the pumpbox. The pump  160  also has an outlet  164 , which may be coupled to a conduit for conveying the discharged stream for further processing. The pump  160  also includes the control input  166  for receiving a pump control signal for controlling operation of the pump. 
     In the embodiment shown in  FIG. 1  and  FIG. 2  the collector  110  is configured as a launder having an overflow inlet  112  and a product outlet  114  for producing a product stream. When the first liquid level in the reservoir volume  102  reaches the level of the inlet  112  the lower specific gravity portion which accumulates at the upper surface  148  overflows into the launder and is discharged through the product outlet  114 . Referring back to  FIG. 2 , the overflow inlet  112  thus defines a high liquid level (HLL) for the reservoir volume  102 . 
     In this embodiment, the apparatus  100  also includes a liquid level sensor  170  and an opening  172  in a sidewall  174  of the pumpbox, which permits sensing of the first liquid level in the reservoir volume  102 . The level sensor  170  includes an output  176  for producing a level signal representing a liquid level in the reservoir volume  102 . The apparatus  100  further includes a controller  180  having an input  182  for receiving the level signal from the output  176  of the level sensor  170 . The controller  180  also includes an output  184  for producing the pump control signal for controlling operation of the pump  160 . In one embodiment, the control signal received at the input  166  of the pump  160  may be an analog signal that controls a speed of the pump, and thus the discharge flow rate through the discharge outlet  108 . In other embodiments, the control signal may be a signal having one of two states, including a first state for causing the pump  160  to operate, and a second state for causing the pump to discontinue operation. 
     Referring back to  FIG. 1 , in the illustrative embodiment the pumpbox apparatus includes a plurality of sidewalls  120  supported by a frame  122 , a base  124 , and a back plate  126 , which together define the reservoir volume  102 . The back plate  126  is inclined at an angle to the base  124  to cause solids that settle out from the accumulated liquid to be generally directed toward the discharge outlet  108 . The apparatus  100  may also include a drain outlet  128  located below the discharge outlet  108 . The drain outlet facilitates periodic or selective flushing of the pumpbox for inspection of the apparatus. Note that while the pumpbox apparatus may have a rectangular outline, curved surfaces may be used in connection with the apparatus in another variation to provide further structural strength. 
     The feedstock stream received at the first inlet  104  may be an oil sand slurry including mineral solids such as sand and clay, water, and a bitumen froth. Preferably, the feedstock stream includes a highly aerated bitumen froth. Highly aerated bitumen froth tends to float fast. Advantageously, in one aspect of the invention, the pumpbox apparatus is operative to selectively separate out such a fast floating aerated bitumen froth. 
     In one embodiment the upstream oil sand flow rate of an oil sand feed may be in the range of about 1000 and about 6000 tonnes per hour. The oil sand feed is diluted with water (e.g. process water) to produce a slurry having densities in the range of about 1400 kg/m3 to about 1650 kg/m3, which is received at the first inlet  104 . The water stream received at the second inlet  106  may be re-circulated process water, which may include dispersed solids and at least some residual bitumen. 
     During operation of the pumpbox apparatus  100 , the feedstock stream and the water stream accumulate in the reservoir volume  102  while the controller  180  monitors the liquid level signal produced by the level sensor  170 . When the first liquid level reaches the low liquid level (indicated as LLL in  FIG. 2 ), the controller  180  responds by changing the state of the pump control signal produced at the output  184 , which in turn causes the discharge pump  160  to be activated to cause accumulated liquid in the reservoir volume  102  to be discharged through the discharge outlet  108 . As the first liquid level in the reservoir volume  102  continues to rise, the controller  180  may respond by increasing the speed of the discharge pump  160  to increase the discharge flow rate through the discharge outlet  108 . When the first liquid level reaches the level of the first inlet  104 , the first and second flow velocity regions  144  and  146  are established. Volumetric flow rates through the pumpbox apparatus  100  may be written as follows:
 
 Q   D   =Q   1   +Q   2   Eqn 1
 
where Q D  is the volumetric flow rate through the discharge outlet  108 , Q 1  is the volumetric flow rate in the first region  144 , and Q 2  is the volumetric flow rate through the second region  146 . Assuming a downwardly vertical flow, the volumetric flow rate in the first region  144  may be written as:
 
 Q   1   =Av   1   Eqn 2
 
where A is the cross-sectional area of the reservoir volume  102 , v 1  is the flow velocity in the first region  144 . Rearranging and substituting Eqn 2 into Eqn 1 gives:
 
 Q   2   =Q   D   −Av   1   Eqn 3
 
     For example, at a discharge rate of 2000 m 3 /hour through the discharge outlet  108  in a vessel having a cross-sectional area of 8 m 2 , in order to maintain a velocity v 1  of 5×10 −2  meters per second, the flow rate through the second inlet  106  should be about 560 m 3 /hour. Under these conditions a velocity v 2  in the second region  146  would be about 7×10 −2  meters per second. Advantageously, the reduced first flow velocity v 1  in the first region  144  facilitates flotation of the low specific gravity portion of the feedstock through the first region  144  to the upper surface  148 . Equations 1-3 above are derived under assumption of vertically downward flow. In practice, flow paths through the apparatus  100  will have portions that are not vertically downward. It should thus be appreciated that for accurate calculation the above analysis would need to be applied to actual flow paths through the apparatus. 
     In the embodiment shown, collection of the low specific gravity portion of the feedstock that floats to the upper surface  148  occurs when the first liquid level in the reservoir volume  102  reaches the level of the overflow inlet  112  of the collector  110 . The overflow inlet  112  therefore defines a high liquid level (HLL) for operation of the pumpbox apparatus  100 . Generally, while it may be desirable to always operate the pumpbox apparatus  100  at the HLL in order to facilitate continuous collection of the low specific gravity portion of the feedstock, in practice variations in flow rate of the feedstock stream through the first inlet  104  would necessarily result in deviations from HLL that would require periodic intervention by an operator to adjust the discharge flow rate Q D  and/or the flow rate Q 2  of the water stream. Practically, the operator would seek to maintain the first liquid level in the reservoir volume  102  between a normal liquid level (NLL) located at or above the first inlet  104  and the HLL. The NLL assumes liquid densities are about a nominal fluid density. Aerated bitumen froth, due to the air content, has a lower density hence a higher level than the nominal fluid. Aerated bitumen froth may have a density ranging from about 600 kg/m3 to about 1000 kg/m3. 
     While the first liquid level is maintained between NLL and HLL and the velocity v 1  is maintained below less than about 5×10 −2  meters per second, favorable conditions for flotation of the low specific gravity portion of the feedstock exists and bitumen should accumulate at the upper surface. When the first liquid level is above NLL but below HLL, bitumen may accumulate, but would not be collected. Accumulated bitumen is collected when the various flows permit the first liquid level in the reservoir volume to rise to the HLL. In one embodiment the discharge pump  160  is operated to maintain the first liquid level at an average liquid level of about 75% of the vertical distance between NLL and HLL above the NLL. 
     Referring to  FIG. 3 , a flow diagram of a system for extracting bitumen from a slurry of bitumen, solids, and water according to one embodiment of the invention is shown generally at  200 . The system  200  includes a plurality of generally conically shaped hydrocyclones, including a first hydrocyclone  202 , a second hydrocyclone  204 , and a third hydrocyclone  206 . The first hydrocyclone  202  includes a feed inlet  210 , an overflow outlet  212 , and an underflow outlet  214 . The second hydrocyclone  204  includes a feed inlet  216 , an overflow outlet  218 , and an underflow outlet  220 . The third hydrocyclone  206  includes a feed inlet  222 , an overflow outlet  224 , and an underflow outlet  226 . 
     In general, hydrocyclones operate by receiving a tangentially oriented flow at the feed inlet and a resulting circumferential flow transports heavier solid particles outwardly towards the walls of the hydrocyclone allowing lower specific gravity components and a portion of the water to be extracted as an overflow stream at the overflow outlet. The solids and a remaining portion of the water exit the hydrocyclone at the underflow outlet. Suitable hydrocyclones for the cyclone separation stages include those manufactured by FLSmidth Krebs of Tucson Ariz., USA under the trademark gMAX®. Alternatively, Cavex hydrocyclones marketed by Warman International may be used. 
     The system  200  further includes the pumpbox apparatus  100  shown in  FIG. 1  and  FIG. 2 . The feedstock received at the first inlet  104  of the pumpbox apparatus  100  includes solids and/or minerals in a significant portion, by weight. For example, the feedstock may have a composition of about 5 wt % to about 15 wt % bitumen, about 40 wt % to about 70 wt % solids (including minerals), and about 30 wt % to about 75 wt % water. The pumpbox apparatus  100  generally operates as described above, and a portion of the low specific gravity bitumen in the feedstock that readily floats to the upper surface  148  of the accumulated liquid in the reservoir volume  102  overflows through the product outlet  114 , and forms a first product stream  228 . The remaining water, solids, and a portion of the bitumen is discharged through the discharge outlet  108  of the pumpbox apparatus  100  and forms the feed stream at the feed inlet  210  of the first hydrocyclone  202 . 
     The first hydrocyclone  202  separates the feed received at the inlet  210  and produces a second product stream  230  of low specific gravity bitumen, water, and some fine entrained solids at the overflow outlet  212  and an underflow stream including solids, water, and a bitumen portion at the underflow outlet  214 . The second product stream  230  is mixed with the first product stream  228  to produce a combined product stream  232  from the system  200 , which may be further processed to separate the low specific gravity bitumen components from the water. In general mixing of the second product stream  230  and the first product stream  228  would occur in a conventional pumpbox. 
     The underflow at the outlet  214  is fed to the feed inlet  216  of the second hydrocyclone  204 . The second hydrocyclone  204  further separates the feed into a low specific gravity overflow stream including mostly water, some bitumen, and some fine solids. The overflow outlet  218  of the second hydrocyclone  204  is fed to the second inlet  106  of the pumpbox apparatus  100 , and forms the water stream inlet for the pumpbox. The underflow stream produced by the second hydrocyclone  204  at the outlet  220  and a system process water feed  208  are combined to make up the feed to the inlet  222  of the third hydrocyclone  206 . The combining of these streams may occur in a conventional pumpbox, for example. 
     The third hydrocyclone  206  further separates the feed into an overflow stream including mostly water, some bitumen, and some fine solids which is fed through the outlet  224  to the feed inlet  216  of the second hydrocyclone  204 . The underflow stream produced by the third hydrocyclone  206  at the outlet  226  forms a tailings stream  234  for the system  200 . The tailings stream  234  may be further processed or diverted to a tailings pond for treatment. The feedstock thus flows serially through the first, second, and third hydrocyclones  202 ,  204 , and  206 , while the system process water feed  208  flows through the third hydrocyclone, to the second hydrocyclone, and through the pumpbox apparatus  100  to the first hydrocyclone. The system process water  208  is thus generally counter to the feedstock flow through the system  200 , which serves to improve recovery of bitumen from the feedstock. 
     The reservoir volume  102  of the pumpbox apparatus  100  provides a capacity for buffering the flow of feedstock to the first hydrocyclone  202 , thereby facilitating operation of the hydrocyclones at a desired steady-state flow rate. In one embodiment the cross sectional dimension of the reservoir volume  102  is about 7.3 meters by about 7.3 meters and the capacity of the pumpbox is selected to accommodate flows of between about 1400 kg/m3 to about 1650 kg/m3 with a residence time of about 30 seconds to about several minutes. For illustrative purposes, in one arrangement, the retention time is about 1 minute. Advantageously, the pumpbox apparatus  100  further facilitates collection of a bitumen portion, in the form of aerated bitumen froth, that readily floats to the surface of the accumulated liquid in the reservoir volume  102 . The first, second, and third hydrocyclones  202 ,  204 , and  206  thus operate on feed streams having bitumen requiring more aggressive processing to separate low specific gravity bitumen from the solids. 
     Advantageously, in the event of a failure of a pump, such as the pump  160  shown in  FIG. 2 , the first liquid level in the reservoir volume  102  of the pumpbox apparatus  100  will rise and overflow at the inlet  112  of the collector  110 , facilitating diversion of the feedstock through the outlet  114  to a safe location. Under these conditions solids will accumulate in the reservoir volume, and the overflow at the inlet  112  will include water, bitumen and some solids. 
     In other embodiments, the configuration of the system  200  may be changed to suit a particular feedstock. For example, where it is desired to process a feedstock having a lower portion of solids, the third hydrocyclone  206  may be omitted, in which case the system process water may be provided to feed inlet  216  of the second hydrocyclone  204 , and the underflow  220  of the second hydrocyclone forms the tailings stream for the system  200 . 
     The pumpbox apparatus  100  may also be used in other applications that generally require blending of two or more streams having components of different specific gravity and where it is desired to collect a low specific gravity portion that readily floats upwardly within the accumulated liquid. 
     While specific embodiments of the invention have been described and illustrated, such embodiments should be considered illustrative of the invention only and not as limiting the invention as construed in accordance with the accompanying claims.