巴西专利BR112012027684B1 Method for controlling a shale shaker and shale shaker for the separation of solids from solid-loade

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METHOD FOR CONTROLLING A SHALE SHAKER AND SHALE SHAKER FOR SEPARATING SOLIDS FROM SOLID-LOADED DRILLING FLUIDS Describes a shale shaker for separating solids from solid-loaded drilling fluids, such a shaker. The shale comprises a basket (100) which has a primary screen assembly (122a, 122b) on an upper screen platform (112) and a secondary screen assembly (125a, 125b) on a lower screen platform (113), the basket (100) further comprising a drainage platform (121) for feeding drilling fluids loaded with solids into a primary duct (107A-D) and a secondary duct (108A-D), the primary duct being (107A-D) is used to feed solid-filled drilling fluids into the primary sieve assembly (122a, 122b) and the secondary duct (108A-D) to feed solid-filled drilling fluids to the assembly secondary sieve (125a , 125b), characterized by the fact that the secondary duct (108A-D) comprises a plurality of secondary duct openings (103A-D), to divide the supply of drilling fluids loaded with solids and at least one opening ( ...).
公开号:BR112012027684B1
申请号:R112012027684-0
申请日:2011-04-11
公开日:2020-06-23
发明作者:George Alexander Burnett；Thomas Robert Larson
申请人:National Oilwell Varco, L.P.；
IPC主号:

专利说明:

For the purposes of any US Patent Application derived from this PCT application, this Application claims priority or is a continuation of USSN 12 / 771,201, filed on April 30, 2010, entitled "Equipment and Method for Separating Solids a From Solid Loaded Drilling Fluids ", which is a continuation in part of document 12 / 490,492, filed on June 24, 2009, entitled" Shale Shaker Flow Diverter ", which is a continuation in part of US Patent Application with serial number 12 / 287,709 filed on October 10, 2008, entitled "Systems and Methods for the Recovery of Lost Circulation and Similar Material" incorporated by reference to all that is disclosed.
The present patent application relates to an equipment and method for the separation of solids from a drilling fluid laden with solids and, in particular, but not exclusively, an equipment and method for the separation of solids to from a drilling mud laden with solids. The present invention patent application also relates to a shale shaker and its respective sieve set.
When drilling a well in the construction of an oil or gas well, a drill is arranged at the end of a drilling column, which is rotated to make the well by forming. A drilling fluid known as a "drilling mud" is pumped through the drill string into the drill bit to lubricate the drill bit. The drilling mud is also used to transport the chips produced by the drill bit and other solids to the surface by means of a ring formed between the drilling column and the well. The density of the drilling mud is closely controlled to prevent the well from collapsing and to ensure that drilling is carried out optimally. The density of the drilling mud affects the drill penetration rate. When adjusting the density of the drilling mud, the penetration rate changes to the detriment of the possible collapse of the well. Drilling mud can also transport lost circulating material to seal porous sections of the well. The acidity of the drilling mud can also be adjusted according to the type of formation layers being drilled. The drilling mud contains, inter alia, expensive synthetic oil-based lubricants, and it is therefore normal to recover and reuse the drilling mud used, but this requires, inter alia, that the solids be removed from the drilling mud . This is achieved by processing the drilling mud. The first part of the process is to separate the solids from the solid-loaded drilling mud. This is at least partially achieved with a vibrating separator, such as the shale shakers disclosed in US 5,265,730, WO and WO. Additional processing equipment, such as centrifuges and hydrocyclones, can be used to clean the sludge from solids. The solids are covered with contaminants and waste. It is not uncommon to have 30 to 100 m3 of drilling fluids circulating in a well.
The resulting solids, referred to herein as "drilling debris" are processed to remove substantially all residues and contaminants from the solids. The solids can then be disposed of in landfills or discharged into the sea, in the same environment from which they came. Alternatively, solids can be used as a material in civil construction or have other industrial uses.
Shale shakers generally comprise an open bottom basket, having an open discharge end and a walled solids feed end. A number of rectangular sieves are placed on the open bottom of the basket. The screens can be substantially planar, or have a slight peak. The basket is arranged on springs above a receiver to receive the recovered drilling mud. A bucket or ditch is provided under the open discharge end of the basket. A motor is attached to the basket, which has a drive rotor provided with the weight of a compensation pool. In use, the motor rotates the rotor and the compensation grouping weight, which causes the basket and sieves attached to the said to shake. The sludge laden with solids is fed into the feed end of the basket for the sieves. The stirring motion induces the separation of the drilling mud from the solids, the drilling mud passing through the screens and the solids above the screens. The stirring motion also causes the solids to move along the sieves towards the open discharge end. The recovered drilling mud is received at the receiver for further processing, and the solids pass over the discharge end of the basket into the ditch or bucket.
Rectangular sieves can be arranged at an angle to the horizontal plane, such as a seven degree tilt angle from the feed end to the discharge end of the shale shaker. The angle can be adjustable. Sieves are usually attached to the basket and the basket is adjustable to adjust the angle of the sieves in relation to the horizontal. The flow of the drilling fluid laden with solids can form a puddle on the inclined screens. The action of the vibrating mechanism causes the solids to scale the inclined sieves to the discharge end of the agitator and to the ditch or bucket.
Generally, a vibrating mechanism that induces a circular vibration tends to throw the solids from the sieve into the air in a circular motion. A vibratory mechanism that induces an elliptical movement will cause the solids to move in the direction of the largest ellipse string. A shale shaker having a vibrating mechanism inducing a very thin ellipse is known as a linear shale shaker and induces rapid movement of the solids along the sieve, although the sieve tends to undergo rapid degradation due to the sudden deceleration of the solids when are in the sieve.
Sieves are generally one of two types: wall hooks; and pre-tensioned.
[0009] The "wall hook" sieve comprises several rectangular layers of mesh in a sandwich, usually composed of one or two layers of fine mesh and a supporting mesh having larger mesh holes and heavier gauge wire. The mesh layers are joined to each side margin by a strip that is shaped like an elongated hook. In use, the elongated hook is connected to a tensioning device arranged along each side of a shale shaker. The shale shaker further comprises a set of crowned support elements, which run along the length of the shaker basket, during which the mesh layers are tensioned. An example of this type of screen is disclosed in GB-A-1,526,663. The support mesh can be supplied with or replaced with a panel with openings in it.
The type of pre-tensioned sieve comprises several rectangular layers of mesh, generally comprising one or two layers of fine mesh and a support mesh having larger holes and heavier gauge wire. The mesh layers are pre-tensioned on a rigid support comprising an angular rectangular iron frame adhered to said. The sieve is then inserted into the channels of channel C arranged inside a basket of a shale shaker. An example of this type of screen is disclosed in GB-A-1,578,948 and an example of a shale shaker suitable for receiving pre-tensioned type screens is described in GB-A-2, 176,424.
A problem associated with shale shakers is that the sieves used in the said ones tend to retain, especially when the solids are gummy, such as clay, or of a size close to the size of the sieve mesh. The latter type of retention is known as retention of particles of similar size. Several solutions have been proposed to solve this problem, as described in document GB-A-1,526,663, being a set of sieves with two layers of screening material in a sandwich and that allows the layers of screening material to move independently to dislodge any particles of similar size housed in one of the sieves.
It is advantageous to use fine mesh filters to filter very small particles, for example, between 50 and 200 µm in size or more, without the filter device clogged with small particles. However, it is fine-mesh filters, in particular, that are prone to such unwanted clogging.
It is also advantageous to have a simple and reliable separator to avoid downtime for maintenance and repairs.
It is preferable, in certain circumstances, to retain particles, for example, of a particle size in the range of 50 to 60 p or greater, by means of a filter.
When drilling an oil or gas well, there may be cracks in the well wall. Such cracks can propagate, which could cause structural problems in the well wall and / or allow drilling fluids to escape through those referred to the formation. In addition, if substantial amounts of drilling fluids are lost, the pressure in the drilling fluid in the well may drop, which can cause the well to collapse. Consequently, Well Reinforcement Materials can be added to the circulated drilling fluid. Well Reinforcement Materials comprise large particles. When the drilling fluid circulates around the well wall containing cracks, the large particles become chocked in the cracks, which reduces the likelihood of propagation of these cracks. It is beneficial to recover these large particles and reuse them in the circulated drilling mud. The shale agitators were then modified to solids sized in solid-filled drilling fluids. Such a shale shaker is disclosed in USSN, 492. A range of solids sizes can be extracted using such a shale shaker and recirculated as Well Reinforcement Material in the fresh drilling fluid. It is desirable to keep some small particles, such as barites, which are often found in drilling muds, and thus fine sieves are preferably not very fine as for filtering the drilling mud barites.
According to the present patent application, a shale shaker is provided for separating solids from drilling fluids laden with solids, the shale shaker comprising a basket with a primary sieve assembly on a platform upper sieve and a secondary sieve set on a lower sieve platform, the basket also comprising a feeding platform for the flow of drilling fluid laden with solids into a primary duct and a secondary duct, the primary duct being serves to feed solid-filled drilling fluids to the primary sieve assembly and the secondary duct serves to feed solid-filled drilling fluids to the secondary sieve assembly, characterized by the fact that the secondary duct comprises a plurality of openings in the second duct to divide the supply of drilling fluids loaded with solids and at least one open discharge line to disperse the solid-filled drilling fluids over the secondary sieve assembly.
The Multisizer VSM and PCT Publication No. WO show an overflow spillway as a method of inducing parallel flow through the stirrer. GB publication No. 2 055 597 shows a method for increasing yield, distributing the flow over two screening platforms at different levels, to allow simultaneous processing.
The function of the shale shaker is to remove the solids from the fluid, and the processes and tests have shown that, due to these solids, the method of dividing the flow above can lead to different properties of fluids being processed by one or the other level. As such, it provides different processing efficiencies and, therefore, different processing.
Preferably, the primary duct has a primary duct opening disposed between the plurality of the second duct openings of the secondary duct. Advantageously, the shale agitator further comprises an additional opening of the primary duct, the opening of the primary duct and additional opening of the primary duct interspersing with the plurality of second duct openings in the secondary duct. Advantageously, the shale shaker further comprises a plurality of primary ducts, each having a duct opening, in which the multiplicity of primary duct openings is interspersed with the plurality of second duct openings in the secondary duct.
Preferably, the drilling fluid filled with solids flows along the flow platform in a flow direction, the flow platform having a flow width substantially transversal to the flow direction, the opening being at least one of the primary duct is disposed transversely to a first portion of the flow platform width and the second duct opening is disposed transversely to a second portion of the flow platform width, the first portion not overlapping the second portion.
Advantageously, the at least one primary duct opening corresponds to a plurality of primary duct openings, and at least the second duct opening is a plurality of second duct openings. Preferably, the drilling fluid loaded with solids flows along the flow platform in the direction of flow, the plurality of openings in the primary duct being interspersed with the plurality of openings in the secondary duct, the plurality of openings in the primary duct and secondary arranged substantially perpendicular to the flow direction.
Advantageously, the flow platform has a feed end and a discharge end, the primary and secondary duct openings being disposed at the discharge end of the flow platform. Preferably, the flow platform has a floor and at least one of the openings in the primary and secondary duct being planar with the floor of the flow platform. Advantageously, the other of the primary and secondary duct has an opening of the planar duct with a floor of the outflow platform. The drilling fluid loaded with solids thus does not pass over a spillway and the drilling fluid loaded with solids is divided by means of the primary and secondary sieve platform with a homogeneous consistency. Overflow from a spillway tends to contain more fluids and lower density solids, and fluids left behind the spillway tend to contain high density solids, which tend to be sharp and aggressive, which deplete the screening material quickly. It is advantageous that the sieve sets are exhausted evenly, so that all sieves can be changed at the same time, which reduces the downtime of the shale shaker. Preferably, the opening of the duct is in the form of a planar opening with a floor of the drainage platform. Advantageously, the opening of the duct is perpendicular to the floor of the drainage platform, the opening being defined by a perimeter. Preferably, at least a portion of the perimeter is planar with the floor of the outflow platform, so that all drilling fluid laden with solids passes through the duct openings and nothing is trapped in the outflow platform.
Advantageously, the flow platform further comprises a valve for directing the drilling fluid laden with solids to one of at least the primary sieve platform and to at least the primary and secondary duct opening. Preferably, the flow platform has at least one gate opening in said and the valve is a gate valve comprising a slide gate sliding from the closed position, passing the gate opening to a closing position of the opening. floodgate.
Preferably, the basket further comprises a scalp sieving platform for receiving a scalp screen to remove large solids from said solid-loaded drilling fluid, such that, in use, said solid-loaded drilling fluid flows from the from the above on said flow platform and said large solids pass on said scalp screen. Preferably, the basket also comprises a fourth ticket 870190135679, from / 2019. p. sieve platform, which can be operated in parallel with one or both upper and lower sieve platforms, or can be used with a sieve that has a finer cut-off point for further grading the solids in the drilling fluids loaded with solids. Advantageously, the large solids pass over the scalp screen to: a bucket; and a ditch. Preferably, the trench comprises a drill which moves the solids into a loading hopper of a solid transport equipment, for example, a positive pressure pneumatic transport equipment.
Preferably, the at least one primary screen platform has a screened fluid flow platform below that for collecting and guiding the flow of the screened drilling fluid. Advantageously, the at least one second sieve platform has a sieved fluid flow platform below that for collecting and guiding the flow of the sieved drilling fluid. Preferably, the basket further comprises at least one discharge duct for directing the sieved drilling fluid from the sieved fluid flow platform to a pit arranged under the basket.
Preferably, the at least one primary screen platform is an upper screen platform and the at least one second screen platform is a lower screen platform, at least part of the lower screen platform being arranged by under the upper sieve platform. Advantageously, the at least one primary screen platform is an upper screen platform and the at least one second screen platform is a lower screen platform, the lower screen platform being entirely arranged under the platform. top sieve. Advantageously, a shale shaker, as claimed in any of the preceding claims [sic], wherein said lower screen platform has a lower screen platform base and the upper screen platform has a base of an upper screen platform , with the base of the lower screen platform being arranged completely below said screen platform base. Preferably, both fit in the same basket and cover substantially the same area as the other.
Preferably, the basket further comprises a chute, in which the at least one primary sieve platform has a solids discharge end and the chute is arranged below said to receive the solids. Preferably, the gutter is made of a composite material, although it can be made from a steel sheet or other metal or plastic material. Preferably, the shale shaker further comprises a sump arranged under the basket, the chute being arranged to feed the solids into the sump. Advantageously, the basket further comprises a jet nozzle arranged to spray the drilling fluid sieved into the chute, in order to facilitate the flow of the solids through said. Preferably, the basket also comprises a flexible duct, the solids flowing through the chute into the flexible duct and into the pit. The flexible tube, preferably, part of a side wall of the basket until a pit arranged below said, being that the flexible duct allows the basket to be isolated from the base to avoid the vibrations that pass to the base.
Preferably, the basket further comprises a chute and a diversion plate, in which the at least one primary sieve platform has a solid discharge end and the chute is disposed below that, the diversion plate directing the solids in the gutter. Advantageously, the basket further comprises a chute and a diversion cover, in which the at least one primary sieve platform has a solids discharge end and the chute is disposed below that, the diversion cover preventing that the solids seep into the gutter. Preferably, the shale shaker further comprises a ditch or bucket, the diversion lid directing the solids to the ditch, or bucket.
Preferably, the at least one primary screen platform comprises a primary screen platform on the left and a primary screen platform on the right. Advantageously, the at least one second screen platform comprises a screen platform on the left and right.
Advantageously, the basket has a feed end and a solids discharge end, the at least one primary sieve platform being arranged at an upward angle from the horizontal of the feed end of the basket to the end of discharge of solids. Preferably, the primary and secondary screen platforms are arranged at an elevation angle comprised between three and twelve degrees and more preferably, seven degrees. Advantageously, the basket angle can be adjusted to change the angle of the at least one primary or secondary screen platform. Alternatively, the at least one primary and secondary screen platform are arranged to be horizontal.
Preferably, the shale shaker further comprises at least one primary screen assembly on at least one primary screen platform and at least one screen assembly on at least one second screen platform. Advantageously, the primary sieve assembly has a sieving material over said and the secondary sieve assembly has a sieving material over said, characterized by the fact that the sieving material of the primary sieve assembly is of the same material as the sieving material from the secondary sieve assembly to provide the same cut point. It is more likely that the shale shaker is operating in parallel with this arrangement. Parallel mode tends to be used when large volumes of drilling fluid are required in a drilling operation, such as when drilling a large diameter well, which normally occurs when drilling the first upper part of the well.
Alternatively, the primary sieve assembly has a sieving material over said and the secondary sieve assembly has a sieving material over said, the sieving material of the secondary sieve assembly being thinner than the sieve material. sieving the primary sieve set to provide different cutting points. It is more likely that the shale shaker is running in series mode with this arrangement.
Preferably, the shale shaker also comprises a fixed base, the basket being suspended from the base by at least one spring, the basket further comprising vibrating equipment to vibrate the basket and at least one of the platforms. primary and secondary screen arranged in said.
In the prior art, the use of a spillway initiates a division function in relation to solids. Generally speaking, the largest and heaviest solids sink immediately when they are on an upper platform and only the smallest and lightest solids are dragged by the current along the spillway over the lower platform. Depending on the quantities of these dimensioned solids, an uneven flow regime may occur. If most solids are large and heavy, then the level of the upper sieve will process most solids and suffer inefficient filtration, reduced yield and increased wear. Alternatively, if the volume of the smaller and lighter solids is large, then the load on the lower platform can be increased substantially, again resulting in inefficient filtration, a reduction in yield and an increase in wear.
Preferably, the flow separation would be 50:50 for any level of the platform, and the properties of the fluids would not be altered in such a way that the screen efficiency would be matched; the present invention patent application provides this facility and a means to avoid that sequential / serial filtration is necessary.
The use of a bypass gate is again proposed to facilitate switching between operations in parallel and series modes. When retracting the gate on the flow platform under the scalping platform, the drilling fluid laden with scalped solids seeps from the scalping platform to the primary upper platform, thus inducing only series operations. When inserting the bypass gate, the drilling fluid loaded with scalped solids is directed to the rear channel of the agitator which is divided into a number of equally spaced cavities. The cavities alternate between directing the fluid to the upper primary platform and directing the fluid to the secondary lower platform. Eight wells are shown, but the number of wells can be varied, if the number of wells is reduced, this can make the separation function less efficient, while increasing the number of wells would make the division more accurate in terms of volume. The bypass gate is configured in such a way that the fluid and solids that are transported are able to flow across the full width of the agitator so that it results in a 50:50 chance of entering a primary feed cavity, or in a secondary feed cavity.
The inventors have observed that a function of shale shakers is to remove solids from the fluid and that the processes and tests in the prior art methods of dividing the flow can lead to different fluid properties, being processed at one level or another. As such, it leads to different processing efficiencies and, therefore, different processing.
According to the present patent application, the height of the spillway in the rear channel must be designed in such a way that the excess flow from the upper platform is eliminated and that all excess flow must be directed to the lower platform in such a way that the operator only needs to concentrate on controlling the flow based on the zero fluid discharge from the lower platform. The height of the spillway is defined to ensure that the excess flow is directed to the sieve below, instead of flooding the sieve completely and losing fluid from the sieve discharge, the spillway being normally adjusted to a height corresponding to a margin length of about 300 mm.
The present patent application also provides a method for controlling a shale shaker comprising a base, a basket isolated from the base, the basket comprising a scalp platform having a scalp screen, an upper platform having a screen set and a lower platform having a fine sieve assembly, the upper platform being fed with drilling fluid laden with scalped solids from a feed platform, the upper sieve platform having a feed end and an end discharge system, characterized by the fact that the upper platform comprises a primary duct for feeding the drilling mud loaded with scalped solids to the upper platform and a secondary duct for feeding the drilling mud loaded with scalped solids to the platform bottom, and a spillway located at the feed end, the method comprising the steps of a puddle of drilling fluid laden with scalped solids formed on the upper deck sieve assembly and the excess drilling fluid laden with scalped solids that passes over the spillway of the feed end of the fine sieve assembly of the deck platform bottom sieve. Preferably, this allows an operator to control the agitator by simply observing the bottom platform and controlling the acceleration of the shale shaker or other controllable attributes, such as the angle of the platform, in response to the visualization of solids and / or liquids drilling rig being unloaded from the bottom platform.
Preferably, the spillway is formed by a plurality of ducts. Advantageously, the plurality of ducts is formed by at least one primary duct feeding the drilling fluid loaded with scalped solids to the upper platform and at least one secondary duct feeding the drilling fluid loaded with scalped solids to the lower platform, being that the method comprises the stages of drilling fluid laden with excess scalped solids passing over at least one primary duct to the secondary duct.
Preferably, the drilling fluid laden with scalped solids passes under the flow platform, at the same level as the flow platform or slightly above the flow platform.
The present application also provides for a shale shaker comprising a base, a basket isolated from the base, the basket comprising a scalp platform having a scalp screen, an upper platform having a fine screen set and a lower platform having a finer sieve assembly, the upper sieve platform having a feed end and a solids discharge end, an outflow platform for feeding solid-filled drilling fluids to a primary duct and a secondary duct, the primary duct being used to feed the drilling fluid filled with solids to the fine sieve set and the secondary duct used to feed the drilling fluid filled with solids to the finer sieve set, characterized by fact that a spillway is located between the primary duct and the secondary duct, in such a way that, in use, when a puddle of p scaling-laden drilling forms in the fine sieve assembly of the upper deck, excess scaling-laden drilling fluid passes from the primary duct over the spillway to the secondary duct and to the feed end of the finer sieve set of bottom sieve platform.
Preferably, the primary duct has an opening of the primary duct and the secondary duct has an opening of the second duct, the primary and secondary duct openings being substantially planar with the flow platform. Alternatively, the primary and secondary duct openings are below the plane of the outflow platform. Preferably, the height of the spillway is adjusted to allow a margin length between 100 mm and 500 mm, and more preferably, 300 mm at the discharge end of the upper screens. Advantageously, the spillway height is preferably adjustable to allow a margin length between 0 mm and 1 m [sic] and more preferably between 200 mm and 500 mm.
Advantageously, the spillway is also substantially planar with the outflow platform. Preferably, the spillway is below the level of the drainage platform.
This aspect of the present patent application may have some or all of the other features and / or steps in the methods, as defined in any declaration of the present patent application defined herein.
The present application also provides a method for separating solids from drilling fluids laden with solids using a shale shaker comprising a basket with a flow platform with at least primary and secondary duct opening, at least primary and secondary duct, at least one primary sieve platform and at least a second sieve platform, the method comprising the steps of draining the drilling fluid laden with solids on the flow platform, by means of, at least primary and secondary duct opening for at least the primary and secondary duct, the at least one primary duct directing the drilling fluid laden with solids to the at least one primary sieve platform and being that the at least one secondary duct directs the drilling fluid laden with solids to the second sieve platform.
The present patent application also provides a shale shaker for separating solids from drilling fluids laden with solids, the shale shaker comprising a basket with a scalp sieving platform, at least one scaling platform. primary sieve and at least one secondary sieve platform, the basket further comprising a drainage platform disposed between the scalp sieving platform and at least one primary sieve platform, and a plurality of primary ducts and a plurality secondary pipelines, the plurality of primary pipelines serving to direct the solid-filled drilling fluid to the at least one primary sieve platform and the plurality of secondary ducts to direct the solid-loaded drilling fluid to the platform secondary sieve.
Preferably, the flow platform has at least one gate opening in said and a gate valve comprising a slide gate sliding from a closed position, the gate opening to an open position, opening the gate opening allowing the drilling mud loaded with solids to flow through said. Preferably, the gate opening is placed upstream of the plurality of primary and secondary ducts, in such a way that none or only a little solid-filled drilling fluid reaches the plurality of primary and secondary ducts.
Advantageously, the basket further comprises a sieved fluid flow platform disposed under at least one primary sieve platform, the sieved fluid flow platform having a selector opening in said and a selector gate valve for opening and selectively close the selector opening, selectively allowing the sieved drilling fluid to flow through said to the at least one secondary screen platform.
The present patent application also provides a shale shaker for separating solids from solid-loaded drilling fluids, the shale shaker comprising a base, a basket isolated from the base, the basket comprising a platform scalp on at least one primary platform and at least one secondary platform, the at least one primary platform having a feed end and a solid discharge end, a chute disposed in the basket at the discharge end of, at least one, primary platform and a bypass plate to selectively inhibit and allow the solids discharged from the discharge end of the at least one primary platform into the chute.
Preferably, the shale shaker also comprises a flexible duct, which departs from the chute in a pit arranged under the sieve drilling fluid collection basket.
The present application also provides a method for separating drilling fluids laden with solids with a shale shaker, the shale shaker comprising a base, a basket isolated from the base, the basket comprising a platform scalp having a scalp screen, at least one primary platform having a screen set and at least one secondary platform having a fine screen set, the at least one primary platform having a feed end and a feed end. solid discharge, a chute disposed in the basket at the discharge end of at least one primary platform and a diversion plate, the method comprising the steps of draining drilling mud laden with solids over the scalp screen, solids large ones that pass over the scalp screen and the solid-filled drilling fluid that passes through the scalp platform to the screen assembly of at least one , primary sieve platform, dimensioned solids that pass over the sieve set for the gutter, guided by the bypass plate on the gutter.
Preferably, the method also comprises the flow step of the solids dimensioned from the chute to a pit under the basket, the pit also collecting the drilling fluid sieved by the fine mesh sieves of at least one secondary platform. sieve. Advantageously, the flow of the dimensioned solids is facilitated by a jet of drilling fluid.
This aspect of the present application for a patent may have some or all of the other features and / or steps of methods, as defined in any declaration of the present application for a patent defined in this document.
A figura 1 mostra uma visualização em perspectiva de um equipamento para a separação de sólidos a partir da lama de perfuração carregada de sólidos; A figura 2A é uma visualização lateral esquemática em corte transversal de um equipamento para a separação de sólidos e dimensionamento da lama de perfuração carregada de sólidos, sendo que o equipamento compreende uma base e um cesto; A figura 2B é uma visualização longitudinal do cesto ilustrado na Figura 2A com os conjuntos de crivo contidos no referido; A figura 3 é uma visualização lateral em seção de um cesto de um agitador de xisto, de acordo com o presente pedido de patente de invenção; A figura 3A é uma visualização ampliada de uma parte do cesto ilustrado na Figura 3, com as partes em um modo primário de operação; A figura 3B é uma visualização ampliada de uma parte do cesto ilustrado na Figura 3, com as partes em um modo secundário de operação; A figura 3C é uma visualização longitudinal do cesto ilustrado na Figura 3 com conjuntos de crivo contidos no referido; A figura 4 é uma visualização em perspectiva de uma parte do cesto ilustrado na Figura 3A, com as partes escondidas mostradas, no modo primário de operação que indica o sentido do escoamento da lama de perfuração carregada de sólidos de uma plataforma primária de crivo superior; A figura 5 é uma visualização em perspectiva de uma parte do cesto ilustrado na Figura 3A, com as partes escondidas mostradas, no primeiro modo de operação que indica o sentido do escoamento da lama de perfuração carregada de sólidos de uma plataforma primária de crivo inferior; A figura 6A é uma visualização ampliada em corte transversal de um aparelho de desvio de sólidos do cesto ilustrado na Figura 3, no modo primário de operação; A figura 6B é uma visualização ampliada de um dispositivo de desvio de sólidos do cesto ilustrado na Figura 3, no modo secundário de operação; A figura 7 é uma visualização longitudinal em corte de um agitador de xisto compreendendo o cesto ilustrado na Figura 3, que mostra detalhes de um dispositivo de desvio de sólidos; e A figura 8 é uma visualização lateral do agitador de xisto mostrado na Figura 7 disposto sobre uma fossa, com algumas partes ocultas mostradas. For a better understanding of the present invention patent application, reference will now be made, by way of example, to the attached drawings, in which: Figure 1 shows a perspective view of an equipment for the separation of solids from the drilling mud loaded with solids; Figure 2A is a schematic side view in cross section of an equipment for the separation of solids and dimensioning of the drilling mud loaded with solids, the equipment comprising a base and a basket; Figure 2B is a longitudinal view of the basket shown in Figure 2A with the sieve assemblies contained therein; Figure 3 is a side sectional view of a shale shaker basket, according to the present invention patent application; Figure 3A is an enlarged view of part of the basket illustrated in Figure 3, with the parts in a primary mode of operation; Figure 3B is an enlarged view of part of the basket illustrated in Figure 3, with the parts in a secondary mode of operation; Figure 3C is a longitudinal view of the basket shown in Figure 3 with sieve assemblies contained therein; Figure 4 is a perspective view of a part of the basket illustrated in Figure 3A, with the hidden parts shown, in the primary mode of operation that indicates the direction of flow of the drilling mud loaded with solids from a primary upper sieve platform; Figure 5 is a perspective view of a part of the basket shown in Figure 3A, with the hidden parts shown, in the first mode of operation that indicates the direction of flow of the drilling mud laden with solids from a primary lower screen platform; Figure 6A is an enlarged cross-sectional view of a solids bypass device illustrated in Figure 3, in the primary mode of operation; Figure 6B is an enlarged view of a solids bypass device illustrated in Figure 3, in the secondary mode of operation; Figure 7 is a longitudinal sectional view of a shale shaker comprising the basket illustrated in Figure 3, which shows details of a solids bypass device; and Figure 8 is a side view of the shale shaker shown in Figure 7 arranged over a pit, with some hidden parts shown.

Figure 1 shows an equipment for the separation of solids from a drilling mud loaded with solids, generally referred to as a shale shaker and identified here by reference H. Shale shaker H comprises a base D having an open bottom R arranged over a collection container (not shown) to receive the sieved drilling mud. A basket B is arranged on springs C on the base D, A vibrating equipment E is arranged on the top of the basket B. The vibrating equipment E comprises a rotating electric or hydraulic motor M to compensate for weights hidden inside the box S, which induces a movement in basket D. Upper, upper, lower and lower Al, A2, A3, A4 sieve assemblies are arranged in basket D and fixed to that in grids (not shown), so that the movement induced in the basket is transferred to the screen sets A1, A2, A3, A4. Drilling fluids laden with solids are fed to the A1-A4 sieve sets from a feed chamber F at one feed end of the equipment. The movement induced in the A1-A4 screen sets facilitates the separation of the solids from the drilling mud. The sieved drilling mud passes through the sieve sets to the collection container (not shown) and the solids rise along the sieve sets A1-A4 to a discharge end P from the shale shaker to a ditch, bucket or other chip transfer equipment (not shown).
Figures 2A and 2B show a shale shaker 10 having a base 20 and a basket 30 disposed on the springs (not shown). The basket 30 comprising a scalp platform 11, an upper primary platform 12 and a lower primary platform 13. The upper primary platform 12 has a left side 12a and a right side 12b. The lower primary platform has a left side 13a and a right side 13b. Drilling fluids laden with solids are introduced into a feed end of the shale shaker 14 from a feeder (not shown) to a scalp screen 15 arranged in C-shaped channels 16 of the scalp platform 11. A bladder pneumatic expandable 17 is arranged at the top of the C-shaped channels 16 to hold the scalp screen 15 inside. Alternatively, a wedge can be used to fix the scalp screen 15 in the C-shaped channels 16. The scalp screen 15 comprises a screen 18 with relatively large openings to prevent the passage of larger particles through the primary platform, but allowing the passage of some solids and drilling mud through said. The scalp platform 11 and the screen 15 are arranged on the above with an upward inclination of about one degree from the horizontal, although the scalp screen 15 and the scalp platform 11 can be arranged horizontally, slightly on a slope or slightly upward angle. The vibrating equipment 16a attached to the basket 30 induces movement within it. The movement facilitates the separation of the large solids from the solid-loaded drilling mud and induces movement in the large solids along the scalp screen 15 from the feed end 14 to the discharge end 19 of the shale agitator. Large solids can be captured in a ditch or a means of transport and further processed or used in other operations. The solid-loaded drilling fluid passing through the scalp screen 15 falls onto a flow platform 21, which directs the solid-loaded drilling fluid to the feed end 14 of the screen assemblies 22a and 22b on the upper primary platform 12 A spillway 23 is arranged at the feed end of the primary platform 12 to retain drilling fluids laden with solids. If the level of the solid-loaded drilling fluid increases beyond the height of the spillway 23, the solid-filled drilling fluid passes over the aforementioned to a duct 23 and over the set of sieves 25a and 25b to a primary lower sieve platform 13. The screen sets 22a, 22b and 25a and 25b are preferably of the same type and have the same screen mesh over those.
The gate valve 26 in the form of a sliding platform, is in a closed position to operate the shale shaker in a parallel mode. The sieved drilling mud falls through the sieve assemblies 22a and 22b on the upper sieve platform to a drainage platform 27 and on the closed gate valve 26, and in a duct 28, which operates in parallel with the duct 24. However, duct 28 leads to the bottom of the basket and directly to the collection container (not shown) below that. The solids fall from the discharge end 31 of the upper sieve platform 12 and discharge end 32 of the lower sieve platform 13 into a bucket or other transport equipment to transport the solids for further processing or reuse.
The gate valve 26 can be retracted to allow the drilling mud sieved through the sieve assemblies 22a and 22b on the upper sieve platform 12 to be sieved further through the sieve assemblies 25a and 25b on the lower sieve platform 13. O shale shaker then operates in a serial mode. In this situation, it is preferable to use a finer mesh screen in the screen sets 25a and 25b than the mesh screen used in the screen sets 22a and 22b. The drilling mud sieved by the sieve assemblies 22a and 22b on the upper sieve platform 12 flows into the outflow platform 27 and into a duct 29, which directs the sieved drilling mud over the feed end of the sieve assemblies 25a and 25b on the lower sieve platform part 13. Large solids fall from the discharge end 31 of the upper sieve platform 12 onto a conveyor (not shown), to be transported and mixed in a fresh batch of drilling mud for recirculation. These large solids are used to block the formation of cracks, as has been described previously here. Discharges of solids from the discharge end 32 of the lower screen platform 13 are transported on a separate conveyor or added to a bucket for further processing or use for other purposes.
Referring to Figures 3, 3A, 3C, 4 and 5, a basket 100 of a shale shaker is shown. Basket 100 comprises a scalp platform 111, an upper primary platform 112 and a lower primary platform 113. The upper primary platform 112 has a left side 112a and a right side 112b. The lower primary platform 113 has a left side 113a and a right side 113b. The solid-loaded drilling fluid is introduced at one end of the shale agitator 114 from a feeder (not shown) to a scalp screen 115 arranged in C-shaped channels 116 of the screen set 111. A bladder pneumatic expandable 117 is arranged at the top of the C-shaped channels 116 to hold the scalp screen 115 inside. Alternatively, a wedge can be used to secure the scalp screen 115 to the C-shaped channels 116. The scalp screen 115 comprises at least one layer of screen material 118, such as a wire mesh with relatively large openings, for prevent the passage of larger particles through the primary upper and lower platforms 112 and 113, but allowing some solids and drilling mud to pass through the aforementioned. The scalp platform 111 and scalp screen 115 are disposed on the above in an upward slope of approximately one degree from the horizontal, although the screen sieve 115 and the screen sieve 111 can be arranged horizontally, slightly downhill or on a slightly larger upward angle. The vibrating equipment 116a attached to the basket 100 induces movement within it. The movement facilitates the separation of the large solids from the solid-loaded drilling mud and induces movement of the large solids along the scalp screen 15 [sic] from the feed end 114 to the discharge end 119 of the shale agitator. Large solids can be captured in a ditch, bucket or transport (not shown) and further processed or used in other operations. The solid-loaded drilling fluid that passes through the scalp screen 115 falls onto a flow platform 121, which directs the solid-loaded drilling fluid along a closed delivery gate valve in the form of a gate platform sliding platform distribution system 101, and as shown in Figures 4 and 5, through eight duct openings 102a, 102b, 102c, 102d and 103a, 103b, 103c and 103d of a collecting tube 104 disposed between the side walls 105 and 106 of the basket 100. Preferably, the eight duct openings 102a, 102b, 102c, 102d and 103a, 103b, 103c and 103d are located at or slightly below the drainage platform 121 and the distribution gate platform 101 Openings 102a, 102b, 102c, 102d and 103a, 103b, 103c and 103d can be arranged vertically in the collecting tube 104 with each opening 102a, 102b, 102c, 102d and 103a, 103b, 103c and 103d having a lower nozzle substantially in line with the u slightly below the delivery gate platform 101. The drilling fluid filled with solids flows in approximately equal amounts through duct openings 102a to 102d for ducts 107a to 107d and through openings 103a to 103d for ducts 108a at 108d. Approximately one-eighth of the flow of solid-loaded drilling fluid passes through each of the openings 102a to 102d and 103a to 103d. Ducts 107a and 107b lead to the respective discharge outlets 109a and 109b, discharging the solid-loaded drilling fluid at a feed end of the sieves 122a of the upper primary platform 112. Ducts 107c and 107d lead to the respective discharge outlets 109c and 109d, discharging the solid-filled drilling fluid at a feed end of the screens 122b of the upper primary platform 112. Ducts 108a and 108b join duct 110a and ducts 108c and 108d join duct 110c, discharging the drilling loaded with solids through the discharge opening 110d on the feed ends of the screens 125a and 125b, respectively, of the lower primary platform 113.
The drilling mud sieved by the sieves 122a and 122b falls through the sieves 122a and 122b onto a drainage platform 127 and drains down onto selector gates platforms 126a and 126b, respectively, and into fluid discharge openings 124a, 124b and 124c . The sieved drilling fluid passes through opening 124a and 124b in a fluid discharge duct 124d and is directed to a pit 157 (see Figure 8), with the sieved drilling fluid also passing through opening 124c and to inside the fluid discharge duct 124e which also directs the sieved drilling fluid to the pit 157 (see Figure 8) disposed below the basket 100.
Drilling fluid laden with solids sieved by sieves 125a and 125b falls through sieves 125a and 125b onto a flow platform 128 that discharges the sieved drilling fluid through opening 129 into a pit (not shown) or into a collection container (not shown).
The solids sieved through the screens 122a and 122b and 125a and 125b are discharged over the solids discharge end 130 and 131, respectively, and into a ditch, bucket or other equipment for collecting solids or means of transport.
In this "in parallel" mode of operation, both the upper and lower sieve platforms are used to filter the same drilling fluids laden with solids, which simply had large solids removed by the 115 scalp sieve. Thus, in this parallel mode, the sets sieves 122a, 122b and 125a and 125b are preferably of the same type and have the same sieve mesh in said.
Referring to Figure 3B, a "series" mode of operation is shown. The delivery gate platform 101 and the selection gate platforms 126a and 126b are retracted. The distribution gate platform 101 is arranged on a grid 132. The distribution gate platform 101 is retracted along the grid 132 by activating a driver (not shown), which can be hydraulic, pneumatic, electrical or mechanical. and can be activated by a key (not shown) on the shale shaker or via the remote control from a control room. The selector gates platforms 26a and 126b are arranged in the respective sets of grids 133a and 133b. The selector gates platforms26a and 126b are retracted simultaneously along the sets of grids 133a and 133b by activating a trigger (not shown), which can be hydraulic, pneumatic, electrical or mechanical and can be activated by a key (no shown) on the shale shaker or via a remote control from a control room.
In this "in series" mode, the distribution gate platform 101 and the selector gate platforms 126a and 126b are retracted revealing an opening 134. The solid-loaded drilling fluid flows through the opening 134 along a bypass platform upper 135 and over the feed end of one of the sieves 122a and 122b on the upper sieve platform 112. The sieved drilling fluid that flows through the sieves 122a and 122b, flows into the flow platforms 127 and through an opening 136 revealed by the selector gates platforms 126a and 126b retracted along a lower deflection platform 137 on the feed end of one of the screens 125a and 125b on the lower screen platform 113.
In this "in series" mode of operation, screens 122a and 122b on the upper screen platform 112 are used for the first "cut" to remove larger solids and screens 125a and 125b on the lower screen platform 113 are used to make a finer cut. Thus, in series mode, screens 125a and 125b will have a finer mesh size than screens 122a and 122b. The solids removed by sieves 122a and 122b are therefore large solids, which can be reused in the sieved drilling mud. Large solids are useful to, among other things, be used as Well Reinforcement Materials to accommodate or block cracks in the well walls as the drilling mud is in circulation.
In use, a puddle of drilling fluid laden with scalped solids can be formed in the sieves 122a and 122b of the primary sieve platform 112. It should be noted that the top of the drilling fluids laden with sieved solids will move the ducts 107A- D substantially in line with the top of the puddle on the primary top screen 112. The excess drilling fluid laden with scalped solids will pass through spillways 200A to 200G from ducts 107A-D to ducts 108A-D and thus excess drilling fluid laden with scalped solids will flow from said to a feed end of the lower primary platform 113.
Figure 6A shows in cross section the solids discharge end of basket 100, taken through side 112a. The solids are transported upwards along the upper surface of the screens 122a and 122b by the vibratory movement induced in the screens 122a and 122b of the vibrating equipment 116. The solids fall from the screens 122a and 122b on the respective parallel baffles 150 (only shown on the side 112a) mounted on a rail 151 and rail 151a. The parallel bypass plate 150 is folded about 25 degrees from the horizontal to facilitate directing the solids out of the basket and into the ditch, bucket or means of transporting the solids. The parallel bypass plate 150 is mounted on top of the rail 151, preferably when the shale shaker is in parallel operation mode.
Figure 6B shows the bypass plate 150 removed and replaced by the series baffles 152 and 152a installed at the end of the basket 100. The series baffles 152 and 152a are mounted on the discharge end of the basket 100 to direct the solids from from screens 122a and 122b to channels 151 and 151a. The flow of solids through the channel 151 and 15a [sic] which has a floor 153, 153a, which slopes in the direction of the respective openings 154 and 154a on sides 105 and 106. The flexible duct connectors 155 and 155a lead to from the openings 154 and 154A, respectively, to the pit channels 156 and 156A on a base 158. The basket 100 is isolated from the base 158 on four springs 159 and 159a (only two are shown). Pit channels 156 and 156a lead to pit 157 below basket 100. Generally smaller solids that are discharged from the discharge end 131 of the lower screen platform 113 fall into the ditch, bucket or other solid transport equipment. to be disposed of or further processed for industrial or construction purposes. Thus, the solids dimensioned between the scalp platform and the primary upper screen are returned to the drilling mud sieved in the pit 157 to be recirculated in a well. The flow of solids through the channels 151 and 151a is facilitated by the total spraying of the drilling fluid sieved through the jet nozzles 160 and 160a, respectively. The jet nozzles are connected to drilling mud supply hoses (not shown) and a pump (not shown). Jet nozzles 1162 are also provided in the channels 1156 of the pit after coupling the flexible duct 11156 to facilitate the flow of solids into the pit 1157.

权利要求:
Claims (5)
[0001]
"METHOD FOR CONTROLLING A SHALE SHAKER", having a base (D), a basket (100) isolated from the base (D), the basket (100) having a primary sieving platform (111), having a primary thick sieve ( 115), an upper platform (112), having a set of screens (122a, 122b) and a lower platform (113), having a set of finer screens (125a, 125b), the upper platform (112) being fed with drilling fluid loaded with solids sieved from a fluid tray (121), the upper sieving platform (112) having a feed end and a solids discharge end, characterized by the feed flow tray (121), at least one primary duct (107A-D) from the shale agitator and at least one secondary duct (108A-D) from the shale agitator, or one primary duct (107A-D) for feeding the drilling mud loaded with solids sieved from the drain pan (121) to the upper platform (112) and the secondary duct io (108A-D) for feeding the drilling fluid laden with solids sieved to the lower platform (113) and a dam (200A-G) located at the feed end between said primary duct (107A-D) and said duct secondary (108A-D), the method taking the steps of when a lagoon of drilling fluid loaded with sieved solids is formed in the sieve assembly (122a, 122b) of the upper platform (112) and in the primary duct (107A-D) , the drilling fluid loaded with excess sieving passes over the dam (200A-G) to the secondary duct (108A-D) and to the feed end of the finer sieve set (125a, 125b) of the sieving platform bottom (113).
[0002]
"SHALE SHAKER FOR THE SEPARATION OF SOLIDS FROM DRILLING FLUIDS LOADED WITH SOLIDS", having a base (D), a basket (100) isolated from the base (D), the basket (100) having a primary screening platform (111), having a primary coarse sieve (115), an upper platform (112), having a set of fine sieves (122a, 122b) and a lower platform (113), having a set of thinner sieves (125a, 125b ), the upper sieving platform (112) having a feed end and a solids discharge end, a drain pan (121) for feeding solid-loaded drilling fluid to a primary duct (107A-D) of the agitator of shale and for a secondary duct (108A-D) of the shale shaker, the primary duct (107A-D) for feeding solid-filled drilling fluid to the fine sieve set (122a, 122b) and the secondary duct (108A -D) for feeding drilling fluid loaded with solids to the set of p finer lines (125a, 125b), characterized by a dam (200) located at the feed end between the primary duct (107A-D) and the secondary duct (108A-D), so that, in use, when a lagoon of drilling fluid filled with sieves forms in the set of fine sieves (122a, 122b) of the upper platform (112), the drilling fluid filled with solids sieved in excess passes from the primary duct (107A-D) over the dam (200) for the secondary duct (108A-D) and for the feed end of the set of finer sieves (125a, 125b) of the lower sieving platform (113).
[0003]
"SHALE SHAKER FOR THE SEPARATION OF SOLIDS FROM DRILLING FLUIDS LOADED WITH SOLIDS", according to claim 2, characterized in that the primary duct (107A-D) has an opening (102A-D) and the secondary duct ( 108A-D) have a secondary duct opening (103a-D), the primary and secondary duct openings being substantially planar to the drain pan (121).
[0004]
"SHALE SHAKER FOR SEPARATING SOLIDS FROM SOLID LOADED DRILLING FLUIDS", according to claim 2, characterized in that the dam (200) is also substantially planar with the drain pan (121).
[0005]
"SHALE SHAKER FOR THE SEPARATION OF SOLIDS FROM DRILLING FLUIDS LOADED WITH SOLIDS", according to claim 2, characterized in that the dam (200) is below the level of the drain pan (121).

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同族专利:

公开号 | 公开日

WO2011135325A3|2013-04-25|

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MX338439B|2016-04-18|

MY155054A|2015-08-28|

CN103153488B|2017-07-28|

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EP3417952A1|2018-12-26|

CA2856188C|2017-11-07|

US20100270216A1|2010-10-28|

WO2011135325A2|2011-11-03|

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AU2011247071B2|2015-02-05|

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EP3415244A1|2018-12-19|

CN105107735A|2015-12-02|

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CA2856191A1|2011-11-03|

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SG2014007736A|2014-03-28|

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BR112012027684A2|2017-07-25|

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法律状态:
2017-08-01| B15I| Others concerning applications: loss of priority|

2017-10-10| B12F| Appeal: other appeals|

2017-10-10| B150| Others concerning applications: publication cancelled|

2019-10-01| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|

2020-05-05| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

2020-06-23| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 11/04/2011, OBSERVADAS AS CONDICOES LEGAIS. |

优先权:

申请号 | 申请日 | 专利标题

US12/771,201|2010-04-30|

US12/771,201|US9079222B2|2008-10-10|2010-04-30|Shale shaker|

PCT/GB2011/050714|WO2011135325A2|2010-04-30|2011-04-11|Apparatus and method for separating solids from a solids laden drilling fluid|

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