Patent Description:
Oilfield drilling fluid, often called "mud," serves multiple purposes in the industry. Among its many functions, the drilling mud acts as a lubricant to cool rotary drill bits and facilitate faster cutting rates. The mud is mixed at the surface and pumped downhole through a bore of the drill string to the drill bit where it exits through various nozzles and ports, lubricating and cooling the drill bit. After exiting through the nozzles, the "spent" fluid returns to the surface through an annulus formed between the drillstriug and the drilled wellbore.

Furthermore, drilling mud provides a column of hydrostatic pressure, or head, to prevent "blow out" of the well being drilled. This hydrostatic pressure offsets formation pressures thereby preventing fluids from blowing out if pressurized deposits in the formation are breeched. Two factors contributing to the hydrostatic pressure of the drilling mud column are the height (or depth) of the column (i.e., the vertical distance from the surface to the bottom of the wellbore) and the density (or its inverse, specific gravity) of the fluid used. Various weighting and lubrication agents are mixed into the drilling mud to obtain the right mixture for the type and construction of the formation to be drilled. Increasing the amount of weighting agent solute dissolved in the mud base will generally create a heavier drilling mud. Drilling mud that is too light may not protect the formation from blow outs, and drilling mud that is too heavy may over invade the formation. Therefore, much time and consideration is spent to ensure the mud mixture is optimal. Because the mud evaluation and mixture process is time consuming and expensive, drillers and service companies prefer to reclaim the returned drilling mud and recycle it for continued use.

Another significant purpose of the drilling mud is to carry the cuttings away from the drill bit to the surface. As a drill bit pulverizes or scrapes the rock formation at the bottom of the borehole, small pieces of solid material are left behind. The drilling fluid exiting the nozzles at the bit stir up and carry the solid particles of rock and formation to the surface within the annulus between the drillstring and the borehole. Therefore, the fluid exiting the borehole from the annulus is a slurry of formation cuttings in drilling mud, and the cutting particulates must be removed before the mud can be recycled.

One type of apparatus used to remove cuttings and other solid particulates from drilling mud is commonly referred to in the industry as a "shale shaker. " A shale shaker, also known as a vibratory separator, is a vibrating sieve-like table upon which returning used drilling mud is deposited and through which substantially cleaner drilling mud emerges. Typically, the shale shaker is an angled table with a generally perforated filter screen bottom. Returning drilling mud is deposited at the top of the shale shaker. As the drilling mud travels down the incline toward the lower end, the fluid falls through the perforations to a reservoir below thereby leaving the solid particulate material behind. The combination of the angle of inclination with the vibrating action of the shale shaker table enables the solid particles left behind to flow until they fall off the lower end of the shaker table. The above described apparatus is illustrative of one type of shale shaker known to those of ordinary skill in the art. In alternate shale shakers, the top edge of the shaker may be relatively closer to the ground than the lower end. In such shale shakers, the angle of inclination may require the movement of particulates in a generally upward direction. In still other shale shakers, the table may not be angled, thus the vibrating action of the shaker alone may enable particle/fluid separation. Regardless, table inclination and/or design variations of existing shale shakers should not be considered a limitation of the present disclosure.

Preferably, the amount of vibration and the angle of inclination of the shale shaker table are adjustable to accommodate various drilling mud flow rates and particulate percentages in the drilling mud. After the fluid passes through the perforated bottom of the shale shaker, it may either return to service in the borehole immediately, be stored for measurement and evaluation, or pass through an additional piece of equipment (e.g., a drying shaker, a centrifuge, or a smaller sized shale shaker) to remove smaller cuttings and/or particulate matter.

Screens used with shale shakers are typically emplaced in a generally horizontal fashion on a generally horizontal bed or support within a basket in the shaker. The screens themselves may be flat or nearly flat, corrugated, depressed, or contain raised surfaces. The basket in which the screens are mounted may be inclined towards a discharge end of the shale shaker. The shale shaker imparts a rapidly reciprocating motion to the basket and hence the screens. Material from which particles are to be separated is poured onto a back end of the vibrating screen, flowing toward the discharge end of the basket. Large particles that are unable to move through the screen remain on top of the screen and move toward the discharge end of the basket where they are collected. The smaller particles and fluid flow through the screen and collect in a bed, receptacle, sump, or pan beneath the screen.

In some shale shakers a fine screen cloth is used with the vibrating screen. The screen may have two or more overlaying layers of screen cloth or mesh. Layers of cloth or mesh may be bonded together and placed over a support, supports, or a perforated or apertured plate. The frame of the vibrating screen is resiliently suspended or mounted upon a support and is caused to vibrate by a vibrating mechanism (e.g., an unbalanced weight on a rotating shaft connected to the frame). Each screen may be vibrated by vibratory equipment to create a flow of trapped solids on top surfaces of the screen for removal and disposal of solids. The fineness or coarseness of the mesh of a screen may vary depending upon mud flow rate and the size of the solids to be removed.

While there are numerous styles and sizes of filter screens, they generally follow similar design. Typically, filter screens include a perforated plate base upon which a wire mesh, or other perforated filter overlay, is positioned. The perforated plate base generally provides structural support and allows the passage of fluids therethrough, while the wire mesh overlay defines the largest solid particle capable of passing therethrough. While many perforated plate bases are generally flat or slightly curved in shape, it should be understood that perforated plate bases having a plurality of corrugated or pyramid-shaped channels extending thereacross may be used instead. In theory, the pyramid-shaped channels provide additional surface area for the fluid-solid separation process to take place, and act to guide solids along their length toward the end of the shale shaker from where they are disposed.

The separation of drilling fluid and other solids from drill cuttings using a screen shaker is often incomplete, resulting in wet drill cuttings. As described above, the drilling mud is introduced to the top of the screen and allowed to flow downward through the screen by gravity alone. Often, additional equipment, such as additional screen separators, hydrocyclones, dryers, drying shakers, centrifuges, hydrocyclone shakers, thermal desorption systems, and other equipment, are used to further dry the cuttings and recover drilling fluid. For example, cuttings from a shale shaker may fall onto a rotary vacuum dryer, where the cuttings travel on a circumferentially rotating screen. Air may be used to strip drilling fluid off the cuttings and into the screen, such as by pulling a vacuum from the interior of the rotating screen (for example, the ROTAVAC™Rotary Vacuum Dryer fluid recovery and cuttings drying system, available from Halliburton).

It is desired to improve the rate and efficiency at which shakers remove liquid from cuttings or other solids. To enhance the gravity-driven separation as described above, it is known that increasing the head on the shaker can increase the throughput of fluids through the screen. Increasing the pressure differential through the screen will likewise increase the fluid capacity of the shaker.

One example of a shaker with increased pressure differential is disclosed by Hensley et al. Hensley et al. disclose an integrated, transportable cutting treatment system, where a pressure differential is developed across the screens to increase the flow rate of drilling mud through the screens. Hensley et al. use an air pump to develop a vacuum beneath the screens to draw mud through the screens. However, applying a continuous vacuum beneath a screen to draw fluid through the screen may result in solids sticking to the screen, hindering the conveyance of solids off the end of the shaker as needed, thereby preventing fluids from being filtered through the screen. <CIT> may be regarded as background art useful for understanding the description.

<CIT> describes a method for the separation of granulate and water in an after-treatment section following a granulator in which a vibrating screen receives the water and granulate mixture, and discloses the preamble of claims <NUM> and <NUM>. In order to obtain low residual moisture without subsequent drying, the granulate-water mixture on the screen is subjected briefly to a vacuum over the entire width of the vibrating screen at longitudinally spaced locations, in alternation, from above and below the screen within the first third of the length of the screen. <CIT> describes a method for separation of liquids from a mixture of solid matter and liquids by supplying the mixture to a separation member which is permeable by liquid, simultaneously applying a vacuum to the underside of the separation member and subjecting the separation member to vibrations.

There exists a continuing desire for shakers having increased fluid capacity, increased fluid flow-through rates across the screens, and/or improved fluid removal efficiencies. Accordingly, there exists a need for a shaker with increased pressure differential. Preferably, the means used to increase the pressure differential do not substantially hinder the flow of solids across the screen deck. Additionally, there exists a need for a shaker for removing entrained gases from the recovered drilling fluid.

The present invention resides in systems as defined in claims <NUM> and <NUM> and in methods as defined in claims <NUM> and <NUM>.

Aspects and advantages will be apparent from the following descriptionand the appended claims.

The accompanying drawings illustrate presently exemplary embodiments of the disclosure, and together with the general description given above and the detailed description of the exemplary embodiments given below, serve to explain, by way of example, the principles of the disclosure.

In one aspect, embodiments and examples disclosed herein relate to a method for separating components of a slurry. As used herein, a slurry refers to a mixture of drilling fluid and drill cuttings. A slurry may be separated using a screen separator having a pressure differential across the screen. In other aspects, embodiments disclosed herein relate to a system for separating components of a slurry. The system includes, a vibratory screen separator and a pressure differential device or a vacuum generating device. The pressure differential device may additionally provide a driving force to degas the recovered drilling fluid.

<FIG> and <FIG> illustrate one embodiment of a vibratory screen separator. The separator <NUM> includes a base <NUM> having four legs <NUM> and supporting members <NUM>. Mounted on the four legs <NUM> are resilient mounts <NUM>. Each mount <NUM> includes a spring <NUM>, a base <NUM> on each leg <NUM> and a socket <NUM> on the separator to receive each spring <NUM>. Positioned on the base <NUM> by the resilient mounts <NUM> is a separator frame or basket <NUM>. The basket <NUM>, includes sidewalls <NUM> and <NUM> and a back wall <NUM>. The front side, opposite to the back wall <NUM>, may be left open. The basket <NUM> is of sufficient structure to withstand the vibrational loads imposed on the basket <NUM> in operation. Extending across the interior of the basket <NUM> between the sidewalls <NUM> and <NUM> is a structural tube <NUM> which may be positioned at roughly the center of mass for further structural strength.

Located about the sidewalls <NUM> and <NUM> and the back wall <NUM> is a channel <NUM>. Located above the channel <NUM> on the sidewalls <NUM> and <NUM> are stops <NUM> and <NUM>. The stops cooperate with the channel <NUM> through its extent along the sidewalls <NUM> and <NUM> to form a screen mounting in a first plane. A screen <NUM> having a screen frame <NUM> and screen cloth <NUM> is illustrated positioned in the screen mounting. Resilient members <NUM> are positioned on the underside of the stops <NUM> and <NUM> to help locate, seat and seal the screen frame <NUM>. Obviously, multiple screens <NUM> may be employed in any one separator.

A sump <NUM> is located below the screen mounting to receive material passed through the screen <NUM>. An inlet <NUM> is positioned at the back wall <NUM> above the screen mounting. An outlet <NUM> for material passed through the screen <NUM> receives material from the sump <NUM> for discharge. Material not passing through the screen <NUM> is discharged off the end of the screen <NUM> and suitably collected. The flow across the screen plane from the inlet <NUM> toward the outlet <NUM> defines a linear direction of material travel. Attached to the sides of the basket <NUM> and specifically to each sidewall <NUM> and <NUM> are two rotary eccentric vibrators <NUM> and <NUM>.

As illustrated in <FIG> and <FIG>, sump <NUM> maybe integrally connected to basket <NUM>. Thus, sump <NUM> may be referred to as a vibrating sump. In other embodiments, sump <NUM> may be separate from basket <NUM>, a stationary sump.

A pressure differential device (not shown) is provided to create a pressure differential between the vapor space above screen <NUM> and the vapor space between screen <NUM> and sump <NUM>. In some examples that do not form part of the invention, the pressure differential
device may be located internal to sump <NUM>, such as an air pump (not shown). In embodiments of the invention, the pressure differential device is located external to sump <NUM>, such as a vacuum system (not shown). Whether internal or external to sump <NUM>, the pressure differential device may cause vapor to flow from the vapor space between screen <NUM> and sump <NUM> to a point external to sump <NUM>, such as through outlet <NUM> or other conduits forming an outlet from sump <NUM>.

The pressure differential device may include, in some embodiments, pumps, blowers, aspirators, ejectors, and the like, and combinations thereof. In various embodiments, the pressure differential may be created by one or more of a positive displacement pump, a momentum transfer pump, or an entrapment pump.

Pumps useful in creating the pressure differential or vacuum in some embodiments include reciprocating pumps, centrifugal pumps, vacuum pumps, pneumatic pumps, electric pumps, air pumps, piston pumps, rotary piston pumps, rotary vane pumps, screw pumps, scroll pumps, liquid ring pumps, external vane pumps, Wankel pumps, Toepler pumps, and Venturi vacuum pumps, among others. Blowers useful in creating the pressure differential may include booster pumps, a rotary lobe blower (such as a ROOTS<™>blower), and vacuum blowers. Useful ejectors and aspirators may include steam ejectors, water aspirators, or ejectors and aspirators utilizing other motive fluids. In some embodiments, drilling fluid is used as the motive fluid for an ejector or an aspirator.

In embodiments of the invention, the pressure differential is pulsed, toggled, or intermittently interrupted. Toggling or pulsing of the pressure differential, as used herein, refers to the changing of the pressure differential from static (a zero pressure differential across the screen) to at least a partial vacuum below the screen. In some embodiments, the pressure differential may be toggled from static to at least a partial vacuum. In other embodiments, the pressure differential across a screen may be toggled or pulsed from static to a full vacuum below the screen. In some embodiments, the pressure differential may be toggled from static to a pressure differential in the range from about -<NUM> to about -<NUM> bar, as given by a quantity defined as a pressure below the screen minus a pressure above the screen. In other embodiments, the pressure differential may be toggled from static to a pressure differential in the range from about -<NUM> to about -<NUM> bar, as given by a quantity defined as a pressure below the screen minus a pressure above the screen; from static to a pressure differential in the range from about -<NUM> to about - <NUM> bar in other embodiments; and from about -<NUM> bar to about -<NUM> bar in yet other embodiments. By toggling the pressure between vacuum and static, conveyance of solids across the screen may proceed unhindered, thereby avoiding solids accumulating or sticking on the screen, and thus not preventing fluid flow through the screen.

Pulsing or toggling the pressure differential between static and vacuum below the screen, in some examples that do not form part of the invention s, may be effectuated by a valve disposed between the pressure differential device (pumps, ejectors, etc., as described above) and the screen. Manipulating the valve by opening and/or closing the valve, at least partially, disrupts the flow of vapor from the sump, thereby affecting the pressure differential. In embodiments of the invention, the toggling device, such as a valve, is disposed between a vacuum generating device or system and the sump located under one or more of the screens.

Valves useful for toggling the pressure differential may include rotary valves, ball valves, globe valves, needle valves, butterfly valves, gate valves, plug valves, diaphragm valves, and piston valves, among others. The valves may be manually operated in some embodiments, or may be remotely actuated valves in other embodiments.

In some embodiments of the pulsed-vacuum assisted screening device disclosed herein, the separator may include two or more screens. One or more sumps are located under the screens such that a pressure differential is
provided across less than all of the two or more shaker screens. In other embodiments, the same or different pressure differentials may be provided across zoned shaker screens.

<FIG> illustrates one example of a pulsed-vacuum assisted screening device having separate pressure zones, where like numerals represent like parts. Separator <NUM> may include two or more screens (not shown), correspondingly located above two or more sumps <NUM> (i.e., 50A and 50B as illustrated). For example, where separator <NUM> has four screens in series, sump 50A may be located proximate inlet <NUM> under the first two screens. Sump 50B may be located proximate outlet 54B, under the last two screens (where first and last corresponds to the direction of flow from inlet <NUM> to outlet 54B). Sump 50A may thus create an independent zone from sump 50B, allowing for operations of the two zones at the same or different pressure differentials. One or more devices may be provided to create a pressure differential across either or both sets of screens. The pressure differential across the screens in either zone may be manipulated to provide additional capacity or to enhance the liquid recovery, resulting in a dryer cutting fraction.

To maintain separate pressure differentials, sumps 50A and 50B may not be in fluid communication. As such, outlet 54A may be provided to discharge material passing through the first two screens into sump 50A.

As described above, one or more pressure differential devices may be provided to create a pressure differential between the vapor space above the screens and the vapor space between the screens and sumps 50A, 50B. In some examples that do not form part of the invention , the pressure differential devices may be located internal to sumps 50A, 50B. In embodiments of the invention, the pressure differential devices are located external to sumps 50A, 50B. Whether internal or external to sumps 50A, 50B, the pressure differential devices cause vapor to flow from the vapor space between the screen and sump 50A, 50B to a point external to each sump 50A, 50B, such as through outlets 54A, 54B, or other conduits forming an outlet from sumps 50A, 50B.

For example, outlet 54A may be used as a liquid outlet, discharging the drilling fluid and other solids passing through screens. An outlet 56A may be provided to convey vapor from sump 50A to create the desired pressure differential. Outlet 56A, in some embodiments, may be connected to a lobe pump <NUM> or to one or more vacuum generating devices as described above. The vapor discharge from vacuum generating device <NUM> may then be vented or further processed, such as through a vapor recovery or incineration system <NUM>.

<FIG> illustrates another example of the pulsed-vacuum assisted screening device. The separator may include a base, legs, supporting members, and other component parts as previously illustrated for mounting separator frame <NUM>. Separator frame <NUM> may include sidewalls <NUM>, <NUM> and a back wall <NUM>. The front side <NUM>, opposite to the back wall <NUM>, may be left open. The frame <NUM> may be of sufficient structure to withstand the vibrational loads imposed on the frame <NUM>. Extending across the interior of the frame <NUM> between the sidewalls <NUM>, <NUM> may be a structural tube <NUM> which may be positioned at roughly the center of mass, for further structural strength.

Located about the sidewalls <NUM> and <NUM> and the back wall <NUM> is a channel (not shown). Located above the channel on the sidewalls <NUM> and <NUM> are stops <NUM> and <NUM>. The stops cooperate with the channel (not shown) through its extent along the sidewalls <NUM> and <NUM> to form a screen mounting in a first plane. A screen <NUM> is illustrated positioned in the screen mounting. Multiple screens <NUM> may be employed in any one separator.

One or more shaker screens <NUM> may be installed in, or secured to, the shale shaker frame <NUM> with a wedge block <NUM>. The screen <NUM> is placed on a support rail (not shown) and positioned underneath a stationary wedge guide <NUM> (stop <NUM>). The wedge block <NUM> (stop <NUM>) is then pounded into position so as to secure the screens <NUM> to frame <NUM>. One of ordinary skill in the art will appreciate that the operator often chooses to use a combination of a hammer and a suitable piece of wood in contact with the wedge block <NUM> to deliver sufficient force to fully tighten the wedge block <NUM>. As shown in <FIG>, the wedge block <NUM> may also include a hammer surface <NUM> to aid in installation (as by pounding on surface 94a) and removal (as by pounding on surface 94b).

An inlet (not shown) may be located proximate back wall <NUM>. The solids may then travel on top of the screens toward front side <NUM>. As illustrated, the separator has four screens <NUM>. The drilling mud may be deposited on the first screen 92A.

A sump <NUM> is provided under the first two screens 92A, 92B. As illustrated, sump <NUM> may be integrally formed with frame <NUM>. One or more pressure differential devices, as described above, are provided to generate a pressure differential across screens 92A, 92B. An outlet <NUM> is provided to convey vapor from sump <NUM> to create the desired pressure differential.

Referring now to <FIG>, a simplified flow diagram of a system for generating a pressure differential across a screen and degassing a fluid, according to an embodiment of the present invention disclosed herein, is illustrated. A shaker <NUM> includes a basket <NUM>, shaker screen <NUM>, and sump <NUM>, as described above. A drilling fluid <NUM> to be separated, such as a mixture of drilling mud and drill cuttings, is fed to inlet end A of the shaker <NUM>. Drill cuttings separated from drilling fluid <NUM> is recovered at outlet end B. The drilling mud <NUM> separated from the drill cuttings is collected in sump <NUM>.

To generate the desired intermittent pressure differential across screen <NUM>, the vapor space <NUM> of sump <NUM> is fluidly connected via flow line <NUM> to a valve <NUM> and a pressure differential device <NUM>, as described above. To prevent liquids from entering flow line <NUM> and pressure differential device <NUM>, vacuum system inlet <NUM> is disposed vertically downward, or includes a cover <NUM>, such as to direct fluid away from inlet <NUM>.

Vapors recovered via pressure differential device <NUM> may be flared, vented, or recovered via flow line <NUM>. Fluids <NUM> are recovered from sump <NUM> via flow line <NUM>, and in some embodiments may be directed to a mud tank for further processing and/or recycled to the mud system.

In the embodiment illustrated in <FIG>, the fluid <NUM> collecting in sump <NUM> during the separations may be degassed or partially degassed by the vacuum or partial vacuum generated by pressure differential device <NUM>. Operation of pressure differential device <NUM> results in at least a partial vacuum in sump <NUM>, and may provide a driving force for gases that may be dissolved or entrained in the fluid <NUM> to be separated therefrom.

If necessary, a vent <NUM> may be provided to aid in pressure control of sump <NUM> or to provide means to avoid under-pressure of sump <NUM>, where vent <NUM> may include pressure relief valves and other devices known in the art to provide flow in limited circumstances.

Referring now to <FIG>, a simplified flow diagram of a system for generating a pressure differential across a screen and degassing the recovered fluid, according to an example that does not form part of the invention disclosed herein, is illustrated. A shaker <NUM> may include a basket <NUM>, shaker screen <NUM>, and sump <NUM>, as described above. A drilling fluid <NUM> to be separated, such as a mixture of drilling mud and drill cuttings, may be fed to inlet end A of the shaker <NUM>. Drill cuttings separated from drilling fluid <NUM> may be recovered at outlet end B. The drilling mud <NUM> separated from the drill cuttings may be collected in sump <NUM>.

To generate the desired intermittent pressure differential across screen <NUM>, sump <NUM> may be fluidly connected via flow line <NUM> to a degassing chamber <NUM>, valve <NUM>, and a pressure differential device <NUM>, as described above. Generation of the intermittent pressure differential across screen <NUM> results in both liquids and vapors being pulled from sump <NUM> to degassing chamber <NUM>. The vapors collecting in degassing chamber <NUM> may be recovered via flow line <NUM>, and may be flared, vented, or otherwise recovered via flow line <NUM>. Fluids <NUM> collecting in degassing chamber <NUM> may be recovered via flow line <NUM>, and in some embodiments may be directed to a mud tank for further processing and/or recycle to the mud system. If necessary, a vent <NUM> may be provided to aid in pressure control of degassing chamber <NUM>, where vent <NUM> may include pressure relief valves and other devices known in the art to provide flow in limited circumstances.

The fluid <NUM> collecting in degassing chamber <NUM> during the separation process may be degassed or partially degassed by the vacuum or partial vacuum generated by the pressure differential device <NUM>. Operation of pressure differential device <NUM> results in at least a partial vacuum in degassing chamber <NUM>, and may provide a driving force for gases that may be dissolved or entrained to be separated from the fluid <NUM>. Such degassing that may occur in embodiments described herein may allow for a simplified mud tank system, where vents and other degassing equipment may not be necessary.

As described above, shaker systems described herein may include a pressure differential device or vacuum generating device to generate an intermittent pressure differential across a shaker screen. The vacuum generated by the pressure differential device may provide an additional driving force for separating fluids from drill cuttings, and may additionally remove vapors and entrained gases from the filtered drilling fluid.

Referring now to <FIG>, a perspective view of a vibratory separator <NUM> in accordance with an example that does not form part of the invention is shown. In this example, vibratory separator <NUM> includes a housing <NUM>, a drilling fluid inlet end <NUM>, an outlet end <NUM>, and a plurality shaker screens <NUM>. In the example shown, the plurality of shaker screens <NUM> are assembled in a multi-tier configuration. By vertically stacking multiple shaker screens <NUM>, the footprint of vibratory separator <NUM> is decreased, thereby providing equivalent separating potential while requiring less space. In vibratory separators <NUM> using vertically stacked shaker screens <NUM>, the size of the apertures in the screens may be varied according to each tier. As drilling fluid begins to flow from a top tier of vibratory separator <NUM>, the screen assembly apertures may be substantially greater in size than the apertures of lower screen assemblies. To prevent drilling fluid from falling on lower disposed shaker screens assemblies <NUM>, a series of flowback pans <NUM> may be located under shaker screens <NUM>. Flowback pans <NUM> may be directed to deposit drilling fluid into a sump <NUM>, thereby allowing drilling fluid to be substantially cleaner at each level of processing.

In this example, vibratory separator <NUM> also includes a fume hood/outlet <NUM> connected to housing <NUM>. In one example, the fume hood/outlet <NUM> may include a vacuum system that extracts vapors into the vent hood/outlet <NUM>. As drilling fluid enters vibratory shaker <NUM> through inlet end <NUM>, the drilling fluid falls onto shaker screen <NUM> and is conveyed from inlet end <NUM> to outlet end <NUM> using vibratory motion and pulse-assisted screening devices as described above. As the drilling fluid is conveyed, vapors, including potentially hazardous gases, for example, hydrogen sulfide ("H2S"), entrained in the drilling fluid maybe present.

In this example, fume hood/outlet <NUM> is configured to extract vapors from the drilling fluid as it flows across the shaker screens <NUM>. As vapors and fumes are released in a generally upward direction from the drilling fluid, fume hood/outlet <NUM> may pull the vapors and fumes inward, thereby trapping the potentially hazardous fumes and/or vapors. Those having ordinary skill in the art will appreciate that by using a fume hood, potentially noxious odors/hazardous conditions may be avoided by directing the flow of air into the hood. Once directed into the hood, a number of subsequent steps may be performed to further treat or vent the trapped gases.

One of ordinary skill in the art will appreciate that fume hood/outlet <NUM> may be turned on during any step of the separation process including during normal separation, during cleaning, or substantially continuously. Thus, examples including fume hood/outlets <NUM> may provide for a vibratory separator <NUM> that is substantially enclosed, thereby preventing the escape of hazardous materials and/or vapors into the drilling work space.

In one example, vibratory separator <NUM> may further include one or more pressure differential devices (not shown) to create a pressure differential between a vapor space <NUM> above and between the screens <NUM> and sump <NUM>. In some examples, the pressure differential devices (not shown) may be located internalto sump <NUM>. In other examples, the pressure differential devices (not shown) may be located external to sump <NUM>. Whether internal or external to sump <NUM>, the pressure differential devices (not shown) may cause vapor to flow from the vapor space between the screens <NUM> and sump <NUM> to a point external to sump <NUM>, such as through outlets 54A, 54B (shown in <FIG>). Fume hood/outlet <NUM> may be in fluid connection with outlets 54A, 54B to pull vapors that flow through such outlets 54A, 54B, thereby trapping the potentially hazardous fumes and/or vapors. Vapors and fumes trapped in fume hood/outlet <NUM> may be treated and/or safely removed from vibratory shaker <NUM> thereafter.

In other examples, vibratory separator <NUM> may include one or more pressure differential devices (not shown) to create a pressure differential between a vapor space <NUM> above the screens <NUM> and flowback pans <NUM>. In some examples, the pressure differential devices (not shown) may be located internalto flowback pans <NUM>. In other embodiments, the pressure differential devices (not shown) may be located external to flowback pans <NUM>. Whether internal or external to flowback pans <NUM>, the pressure differential devices (not shown) may cause vapor to flow from the vapor space between the screens <NUM> and flowback pans <NUM> to a point external to flowback pans <NUM>, such as through outlets 54A, 54B (shown in <FIG>). Fume hood/outlet <NUM> may be in fluid connection with outlets 54A, 54B to pull vapors that flow through such outlets 54A, 54B, thereby trapping the potentially hazardous fumes and/or vapors. Vapors and fumes trapped in fume hood/outlet <NUM> may be treated and/or safely removed from vibratory shaker <NUM> thereafter.

In one example, after the drilling fluid passes through shaker screens <NUM>,the drilling fluid may be directed to a containment area where the drilling fluid may be degassed to remove remaining entrained gases. Degassing the drilling fluid may be performed by any method known in the art. For example, mechanical degassers and aeration devices may used, as disclosed in co-pending Application Nos. <CIT> and <CIT>, assigned to the assignee of the present application. A mechanical degasser may exert a centrifugal force on the drilling fluid. The centrifugal force of the mechanical degasser multiplies the force acting on the entrained gas (e.g., H2S) to increase buoyancy of the gas, thereby releasing entrained gas from the drilling fluid. The increase in buoyancy of the gas accelerates the bubble-rise velocity of the gas velocity, and as the gas bubbles rise toward the surface, they escape the drilling fluid. One of ordinary skill in the art will appreciate that any device known in the art that exerts a centrifugal force on the fluid, thereby reducing the amount of entrained or dissolved gases in the process fluid, may be used in place of a mechanical degasser.

Advantageously, embodiments of the invention and examples disclosed herein may provide shakers having increased fluid capacity, increased fluid flow-through rates across the screens, and/or improved fluid removal efficiencies. Also, advantageously, embodiments disclosed herein may provide shakers with reduced hazardous vapors in vaporspaces. Finally, embodiments disclosed herein may provide shakers that more efficiently separate entrained gases from drilling fluids.

Claim 1:
A system for separating components of a slurry, comprising:
a screen (<NUM>) disposed in a vibratory separator (<NUM>);
a sump (<NUM>) disposed below the screen (<NUM>), the sump (<NUM>) configured to receive material that passes through the screen (<NUM>) and comprising an outlet (<NUM>) for discharging collected material;
a flowline (<NUM>) extending inside the sump (<NUM>) and comprising an inlet (<NUM>) disposed within a vapor space (<NUM>) of the sump (<NUM>);
a pressure differential device (<NUM>) in fluid communication with the sump (<NUM>) via the flowline (<NUM>) and configured to generate an intermittent pressure differential between a space above the screen (<NUM>) and a space between the screen (<NUM>) and the sump (<NUM>); and
a valve (<NUM>) coupled between the pressure differential device (<NUM>) and the sump (<NUM>) along the flowline (<NUM>) to adjust the pressure differential;
wherein the pressure differential device (<NUM>) is configured to cause air and or vapor to be pulled from the sump (<NUM>) through the flowline (<NUM>);
characterized in that the inlet (<NUM>) of the flowline (<NUM>) is disposed vertically downward in the sump (<NUM>) to prevent liquids entering the flowline (<NUM>).