Patent Publication Number: US-2022228581-A1

Title: Double acting pump design utilizing two rotating discs

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
     This application claims priority to U.S. Provisional Application No. 62/963,703 filed Jan. 21, 2020 and U.S. Provisional Application No. 63/033,026 filed Jun. 1, 2020. This application also claims priority to Patent Cooperation Treaty US21/14155, dated Jan. 20, 2021, the entirety of which is incorporated by reference. 
    
    
     FIELD OF THE INVENTION 
     Aspects of the disclosure relate to pumps. More specifically, aspects of the disclosure provide for a double acting pump that may be used in fluid transfer applications, wherein the double acting pump utilizes two rotating tapered discs to actuate a piston. 
     BACKGROUND INFORMATION 
     Currently, there are a variety of types of positive displacement pumps (PD) that include single-acting reciprocating pumps. As time has progressed, the demand for efficient pumping systems continues to grow. This growth can be attributed to increasing demand from the oil &amp; gas industry, as these pumps can deliver high pressures needed for oil field activities. Conventional pumps attempt to have a capacity that is not affected by external forces, such as external liquid forces, thus making them an ideal choice at places where the inlet forces are low. One such conventional pump system is illustrated in  FIG. 1 . 
     Positive displacement (PD) pumps are further segmented into reciprocating pumps, rotary pumps, and others. Rotary pumps are different from positive displacement pumps, owing to their ability to facilitate flow even at differentiating pressures and viscosity conditions. They are used in the lubrication of processing equipment, wind turbines, and hydraulic fracturing trucks. 
     In a positive displacement reciprocating pump, through the suction valve, fluid is pushed into the intake stroke cylinder and then, through the outlet valves, it is discharged on the discharge stroke cylinder under positive pressure. There is only one suction valve and discharge valve per cylinder. The discharge is changed only when the pumping speed is changed. Due to its unique character to provide constant discharge, the product is highly popular in industries such as chemical, power, and others. 
     The use of positive displacement pumps is rising globally as its application scope is widening in water treatment, oil and gas, chemical, and food &amp; beverage industries. This is mainly due to the ability of positive displacement pumps to operate effectively under diverse conditions including high viscosity operations, high-pressure operations, and differential flow pressure operations. 
     In a positive displacement rotary pump, the fluid movement is achieved by mechanical displacement of liquid. The liquid displacement is attained by using a rotation principle. The rotation creates a vacuum, which captures and draws the fluid. These products are more efficient as they naturally remove the air present in the lines along with the fluid. 
     Mud pumps used in the oil and gas industry are a positive displacement reciprocating mud pump. These pumps are used extensively throughout the oil &amp; gas industry and have the capability of moving different constituent ‘muds’ for purposes of drilling and well control. 
     Mud pumps are based on a single acting reciprocating pump action, via connecting rods and a crankshaft to provide a forward motion for the piston operation. The number of pistons typically is 3 or 5. 
     There is a need to provide a pump mechanism that is more efficient than conventional direct action pumps. 
     There is a further need to provide a pump mechanism that is easy to manufacture and maintain in field conditions. 
     There is a further need to provide a pumping system/arrangement that may accommodate different types of muds used in the industry. 
     There is a further need to provide a pumping system/arrangement that will have the advantages of single action reciprocating pumps, but that have a greater efficiency compared to such units. 
     SUMMARY 
     So that the manner in which the above recited features of the present disclosure can be understood in detail, a more particular description of the disclosure, briefly summarized below, may be had by reference to embodiments, some of which are illustrated in the drawings. It is to be noted that the drawings illustrate only typical embodiments of this disclosure and are therefore not to be considered limiting of its scope, for the disclosure may admit to other equally effective embodiments without specific recitation. Accordingly, the following summary provides just a few aspects of the description and should not be used to limit the described embodiments to a single concept. 
     In one example embodiment, an arrangement is disclosed. The arrangement may comprise a shaft and two parallel tapered rotating discs bearing mounted on the shaft, such discs configured to rotate with the shaft, wherein a first portion of a first of the two parallel tapered rotating discs maintains a fixed distance between a corresponding second portion of a second of the two parallel tapered rotating discs during rotation of both of the two parallel tapered rotating discs with the shaft. The arrangement may also comprise at least one block arranged in a radial pattern between the two parallel tapered rotating discs; each of the at least one blocks having at least one void in each block. The arrangement may also comprise a piston located within the at least one void in the block, the piston configured to translate from a first position to a second position, between the tapered rotating discs. The arrangement may also comprise a first housing connected to the block, the first housing having a suction side and a discharge side, the first housing configured to channel a fluid. The arrangement may also comprise a second housing connected to the block, the second housing having a suction and a discharge side, the second housing configured to channel the fluid. The arrangement may also comprise at least a first suction check valve and a first discharge check valve located in the first housing. The arrangement may also comprise at least a second suction check valve and a second discharge check valve located in the second housing. 
     In another example embodiment, a method is disclosed. The method may comprise providing a fluid stream to a pump with two rotating tapered discs configured to rotate with a shaft and directing the fluid stream to at least one block having a piston. The method may also comprise rotating each of the two rotating tapered discs with the shaft, causing the at least one piston to translate with the at least one block, such translation creating both a suction and a compression within the block during the translation and moving the fluid stream in the at least one block during each compression stroke of the piston. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
       So that the manner in which the above recited features of the present disclosure can be understood in detail, a more particular description of the disclosure, briefly summarized above, may be had by reference to embodiments, some of which are illustrated in the drawings. It is to be noted, however, that the appended drawings illustrate only typical embodiments of this disclosure and are therefore not to be considered limiting of its scope, for the disclosure may admit to other equally effective embodiments. 
         FIG. 1  is a perspective view of a conventional mud pump. 
         FIG. 2  is a table of performance values of the conventional mud pump illustrated in  FIG. 1 . 
         FIG. 3  is a perspective view of an arrangement that may be used as a double acting pump utilizing two rotating tapered discs in one example embodiment of the disclosure. 
         FIG. 4  is a perspective view of a thrust plate outer housing and connecting equipment. 
         FIG. 5  is a cross-sectional view of the thrust plate outer housing of  FIG. 4 . 
         FIG. 6  is a piston movement representation for the two rotating tapered disc double acting pump arrangement of  FIG. 3 . 
         FIG. 7  is a conventional fluid end arrangement. 
         FIG. 8A  is an arrangement drawing of fluid valves in one example embodiment of the disclosure with fluid flow in a first direction. 
         FIG. 8B  is an arrangement drawing of fluid valves in another example embodiment of the disclosure with fluid flow in a second direction. 
         FIG. 9  is perspective view of a fluid end/check valve arrangement in one non-limiting embodiment of the disclosure. 
         FIG. 10  is perspective view of a block with a void into which a piston is positioned as part of the double acting fluid end rotating thrust plate pump. 
         FIG. 11A  is a cross-section of a piston and block arrangement channeling flow. 
         FIG. 11B  is a cross-section of the piston and block arrangement of  FIG. 11 , during a discharge flow event through the housing. 
         FIG. 12A  is a cross-section of a valve with a fluid flow being processed in a first direction. 
         FIG. 12B  is a cross-section of a valve with a fluid flow being processed in a second direction with the valve internals reversed. 
     
    
    
     To facilitate understanding, identical reference numerals have been used, where possible, to designate identical elements that are common to the figures (“FIGS”). It is contemplated that elements disclosed in one embodiment may be beneficially utilized on other embodiments without specific recitation. 
     DETAILED DESCRIPTION 
     In the following, reference is made to embodiments of the disclosure. It should be understood, however, that the disclosure is not limited to specific described embodiments. Instead, any combination of the following features and elements, whether related to different embodiments or not, is contemplated to implement and practice the disclosure. Furthermore, although embodiments of the disclosure may achieve advantages over other possible solutions and/or over the prior art, whether or not a particular advantage is achieved by a given embodiment is not limiting of the disclosure. Thus, the following aspects, features, embodiments and advantages are merely illustrative and are not considered elements or limitations of the claims except where explicitly recited in a claim. Likewise, reference to “the disclosure” shall not be construed as a generalization of inventive subject matter disclosed herein and should not be considered to be an element or limitation of the claims except where explicitly recited in a claim. 
     Although the terms first, second, third, etc., may be used herein to describe various elements, components, regions, layers and/or sections, these elements, components, regions, layers and/or sections should not be limited by these terms. These terms may be only used to distinguish one element, component, region, layer or section from another region, layer or section. Terms such as “first”, “second” and other numerical terms, when used herein, do not imply a sequence or order unless clearly indicated by the context. Thus, a first element, component, region, layer or section discussed herein could be termed a second element, component, region, layer or section without departing from the teachings of the example embodiments. 
     When an element or layer is referred to as being “on,” “engaged to,” “connected to,” or “coupled to” another element or layer, it may be directly on, engaged, connected, coupled to the other element or layer, or interleaving elements or layers may be present. In contrast, when an element is referred to as being “directly on,” “directly engaged to,” “directly connected to,” or “directly coupled to” another element or layer, there may be no interleaving elements or layers present. Other words used to describe the relationship between elements should be interpreted in a like fashion. As used herein, the term “and/or” includes any and all combinations of one or more of the associated listed terms. 
     Some embodiments will now be described with reference to the figures. Like elements in the various figures will be referenced with like numbers for consistency. In the following description, numerous details are set forth to provide an understanding of various embodiments and/or features. It will be understood, however, by those skilled in the art, that some embodiments may be practiced without many of these details, and that numerous variations or modifications from the described embodiments are possible. As used herein, the terms “above” and “below”, “up” and “down”, “upper” and “lower”, “upwardly” and ‘downwardly’, and other like terms indicating relative positions above or below a given point are used in this description to more clearly describe certain embodiments. 
     As provided herein, embodiments provide for a double acting pump arrangement  10  that has the capability of performance not achieved by conventional apparatus. For purposes of definition, when a piston or rod moves in a fluid in both directions of a piston  12  movement, the action is defined to be “double acting”. Such a configuration is significantly different than conventional pumps that have a “single” action or fluid movement capability in only one direction, such as a compression stroke. Embodiments of the disclosure provide for an arrangement  10  that uses a set of tapered rotating discs  102 ,  104  (2 discs—1 on each end). Such tapered rotating discs  102 ,  104  are illustrated in  FIG. 6 . As provided in this embodiment, the tapered rotating discs  102 ,  104  are connected to individual pistons  12  that run through a block  14  (described in relation to  FIG. 10 ). These pistons  12  have a mechanical connection on one side to a first of the two tapered rotation discs  102  and to a second of the two fixed rotating discs  104 . As the discs  102 ,  104  rotate, the piston  12  is moved within the block  14  from a first position  120  to a second position  130 . The movement of the piston  12  from the first position  120  to the second position  130  pumps fluid based upon which side of the block  14  is experiencing compression. Valving, described later, prevents back flow of fluid into the block  14  once the fluid has been pushed from the block  14 . 
     Referring to  FIG. 3 , a perspective view of the arrangement  10  is illustrated. The arrangement  10  allows for fluid flow through the arrangement  10  during movement of a piston  12 , illustrated in  FIG. 6 , placed within a block  14 , illustrated in  FIG. 10 . The piston  12 , in one non-limiting embodiment, may be actuated by a mechanical actuator. Different types of mechanical actuators may be provided, such as a pump. Fluid is provided to each block  14  by a fluid feeding system  85 . The fluid feeding system  85  may include a header  87  that has individual feed lines  89 A,  89 B,  89 C, etc. transmitting fluid to the block  14 . The fluid feeding system  85  may be computer controlled such that a constant supply of fluid is provided to the pump to prevent fluid starvation. 
     In embodiments, as illustrated in  FIG. 9 , a first housing  16  used in  FIG. 3 , is shown in more detail. As will be understood, numerous housings can be used within an arrangement  10  according to the number of blocks  14  provided. Generally, the number of blocks  14  is an odd number. Each of the blocks  14  is provided with first and second housings  16 ,  18 . The housings  16 ,  18  are provided to house the associated valving to conduct the fluid to and from the arrangement  10 . In one example, housing  16  is provided to house a suction check valve  100 S and a discharge check valve  100 D, wherein the valves are illustrated in  FIGS. 8A and 8B . These check valves  100 S,  100 D are provided to ensure that fluid flow occurs in a specific direction. A second housing  18  is also provided. Two fluid connections are provided between the first housing  16  and the second housing  18 . Fluid may pass through the two fluid connections provided. The second housing  18  provides a second suction check valve  102 S and a second discharge check valve  102 D. The connections are provided such that the suction check valve  100 S links to the second suction check valve  102 S through a spool. The second fluid connection links the discharge check valve  100 D to the second discharge check valve  102 D through a second spool. The first housing  16  and the second housing  18  are connected to the block  14 , through, for example, a first bolted connection  900  (between the first housing and the block  14 ) and a second bolted connection  902  (between the second housing  18  and the block  14 ). 
     In embodiments, the check valves  100 S,  100 D,  102 S,  102 D are self-contained units that may be placed within the first or second housing  16 ,  18  as appropriate. The self-contained units may be a cartridge style unit such that maintenance for the arrangement  10  is superior compared to conventional apparatus. 
     In embodiments, the arrangement  10  may be made of metallic materials to provide for long-term and maintenance free operation. Such materials may be, for example, stainless steel, carbon steel or other similar materials. 
     In embodiments, the arrangement  10  is used to pump a fluid, such as a mud used in oil and gas exploration and recovery operations. The arrangement  10 , as described above, may operate in a double acting fashion. Two discs  102 , 104  are mounted on a shaft  105 . The discs  102 , 104  are located at a known or “fixed” distance apart from the other disc. Each of the discs  102 , 104  are mounted on the shaft  105  through use of a bearing  106 . The rotating discs  102 , 104  are provided such that the discs amount of space between facing portions of the rotating discs  102 ,  104  is the same value. Thus, when the discs  102 ,  104  rotate in the same direction, a piston connected between the discs is move (translate) back and forth during disc rotation. 
     The arrangement  10  is further configured with a number of blocks  14 . Each of the blocks  14  is provided with at least one void  30  within each of the blocks  14 . The blocks  14  are arranged in a pattern between the parallel tapered rotation discs  102 ,  104 . The arrangement  10  may be in a radial configuration. The rotation discs  102 ,  104  have an internal bore that has a spline feature. This spline feature allows the discs  102 ,  104  to engage with the shaft  105 . The splines also allow the thrust plate housing to translate for maintenance purposes, i.e. slide along the spline. The shaft  105  provides the interface for the input drive system, and also makes the connection across the pump between the rotation discs  102 ,  104  to ensure they are synchronously timed with each other. The shaft  105  acts as a connection between the 2 rotation discs  102 ,  104 . 
     Each of the blocks  14 , is provided with a piston  12  that interfaces with the block  14 , wherein the piston  12  is placed within the at least one void  30  of each of the blocks  14 . The piston  12  is configured to move from a first position  120  to a second position  130 . This movement may be, for example, in a linear motion. Each of the blocks  14  is configured to be connected to a first housing  16  with a suction side  22  and a discharge side  24 . In a similar fashion, each of the blocks  14  is configured to be connected to a second housing  18 , each with a suction side  28  and a discharge side  31 . The first  16  and second  18  housings are described above in relation to  FIG. 9 . 
     The piston  12  may move from a first position  120  to a second position  130 . The movement may be achieved though a mechanical connection to the piston  12 . In one embodiment, the mechanical connection is configured such that an end of the piston  12  contacts an associated tapered rotating block. 
     In one non-limiting embodiment, the first housing  16  is connected to the block  14  through a first bolted connection  900 . In one non-limiting embodiment, the second housing  18  is connected to the block  14  through a second bolted connection  902 . Although described as a bolted connection, other connection types are possible and as such, the illustrated embodiment should not be considered limiting. 
     Referring to  FIG. 10 , a block  14  for the arrangement  10  is illustrated. The block  14  is configured with a void  30  that allows a piston  12  to move from a first position  120  to a second position  130  within the block  14 . The piston  12  is configured such that a snug fit is maintained between the piston  12  and the block  14 . In embodiments, the piston  12  may be configured with rings to help provide a tight seal between the piston  12  and the block  14 . The block  14  is configured with a first set of auxiliary holes  70  and a second set of auxiliary holes  72 . The first set of auxiliary holes  70  and the second set of auxiliary holes  72  are configured with a connection with the void  30  such that movement between the first set of auxiliary holes  70  and the void  30  as well as between the second set of auxiliary holes  72  and the void  30 . The first set of auxiliary holes  70  and the second set of auxiliary holes  72  are configured to allow fluid to travel into and out of the block  14  and through valves that will be housed in a first housing  16  and second housing  18 , described later. The valve arrangements may be as described in relation to  FIGS. 8A and 8B , in one non-limiting embodiment. 
     Mud is provided to the pump via a lower suction manifold which distributes the mud to the fluid ends. Typical pump configurations are three (3) fluid ends referred to as a triplex pump or five (5) fluid ends referred to as a quintuplex pump. Mud may be mixed separately from the configurations shown in equipment known in the art. 
     The arrangement  10  is also unique and reconfigured to a radial setup, allowing a greater density of components. For the example illustrated  3  below depicts a 7 piston/7 arrangement. However, any other odd number of pistons and fluid ends ( 3 ,  5 ,  7 , etc.), can be utilized depending on pump pressure and flow volume performance requirements. The design is uniquely flexible, providing a scalable design, based on number of fluid ends; stroking of the piston  12  (movement) and the power capacity available to drive the pump. 
     Two Rotating Tapered Discs 
     Referring to  FIGS. 4, 5 and 6 , two rotating tapered discs  102 ,  104  are used to actuate the piston  12 . The two rotating tapered discs  102 ,  104  are located within the outer housing mounted on bearings  106  to support the loads developed during rotation of the thrust plate. The housing and end cover provide a sealed chamber for oil lubrication. Attached to the lid are a number of guide sleeves. The piston rods  99  reciprocate with the guides. One end of the piston rod  99  as a socket arrangement as the receiving location for the piston rods  99  held within the fluid end. The opposing end of the piston rod  99  is a spherical ball arrangement with allows articulation between the thrust plate angled surface to the piston rod  99  allowing a linear action to be generated. 
     Double Acting Fluid End and Check Valve Arrangement 
     A conventional fluid end arrangement ( FIG. 7 .) has a two (2) item, check valve arrangement. A first check valve on the inlet side, referred to as a suction valve, allows fluid to be drawn into the fluid end via the piston  12  action on the backward stroke. A second check valve on the outlet side, referred to as the discharge valve, allows pressurized fluid flow out of the fluid end. Should a backflow of fluid be caused, the check valves prevent any backflow within the fluid end. 
     For example, as fluid is being drawn into the fluid end, the lower suction check valve allows unrestricted flow. However, as pressure is development within the main fluid end bore via the forward action of the piston  12 , the check valve then seats fully, preventing any fluid flow out through the lower (inlet) aperture. Similarly, the upper discharge check valves allow flow outlet, while preventing any flow into the fluid end via the upper check valve. 
     Aspects of the disclosure provide a different configuration than the conventional apparatus in  FIG. 7 .  FIGS. 8A and 8B  provide a double acting design. As the disclosed embodiment is a double action piston  12  arrangement, pressure and flow can be created in both directions, adding to the efficiency of the pump. By combining four (4) check valves, within the inlet and outlet ports, in one embodiment, the fluid is configured to produce pressure and flow in both piston directions. 
     With a combination of two (2) suction and two (2) discharge check valves, per  FIGS. 8A &amp; 8B , the pressure discharge is available in both directions of the piston  12  movement, while preventing any backflow to the suction side of the arrangement, ensuring discharge flow is in one direction only. To facilitate the block  14  and first  900  and second  902  housings have associated pathways for fluid to be transported. (See,  FIG. 9 ). 
     Check Valve Cartridge 
     Per the description of  FIG. 7 . above for conventional apparatus, check valves are used in the conventional setup, but tend to be ‘disk’ like arrangements, i.e., a disk with elastomer face seats against a mating surface to provide the sealing function. However, as can be seen the flow path can be quite torturous through the valve arrangement, which in some cases causes ‘wash out’—a phenomenon, where the turbulent flow of the fluid starts to erode the flow path walls/components. This results in physical damage to the components meaning they have a reduced service life and require constant maintenance. 
     To address the issue of the check valve wash out, embodiments of the disclosure provide a valve arrangement that eliminates wash out and that can be used in both suction and discharge operations. Additionally, aspects of the disclosure, as illustrated in  FIGS. 8A and 8B , create a smooth flow when the valve is opened for the flow condition, reducing turbulent flow potential, and consequently extending service life. 
     In embodiments, after an extended operation period, it is anticipated the whole check valve cartridge just simply be removed from the main flow body and replaced as a whole, resulting in reduced service requirements. 
     Referring to  FIGS. 11A and 11B , flow paths for fluids being processed through the piston  12  and the first and second housings  900 ,  902  are illustrated. In  FIG. 11A , the direction of the piston  12  is travelling to the right, causing a compression stroke on the right side of the block  14 . Fluid, squeezed between the piston  12  and the block  14  goes under pressure. Movement of the piston  12  to the right, causes a suction flow of fluid on the left side of the piston  12 , through a suction valve. Once fluid pressure at the right increases to a desired level, referring to  FIG. 11B , the discharge valve above the piston  12  to the right opens, allowing the pressurized fluid to exit. As will be understood, the piston  12  will then travel to the left side of the block  14 , thereby pressurizing the fluid. After reaching the desired pressure level, a discharge valve at the left will open, allowing the fluid to escape. During movement of the piston  12  to the left, a suction valve at the right of the block  14  will open, allowing fluid to enter the right side of the piston  12 . 
     Referring to  FIGS. 12A and 12B , a cross-section of the valves used in the arrangement  10  is illustrated. The valves  1200  are cartridge type valves that may be easily installed. Each valve  1200  provides an upper check valve body  1202 , a cartridge body  1204 , a check valve guide  1206 , a lower check valve body  1208  and a check valve body seat  1210 . In  FIG. 12A , flow to the bottom of the valve  1200  causes the lower check valve body  1208  to be positioned as illustrated. In  FIG. 128 , where flow is reversed, the lower check valve body  1208  is repositioned as illustrated. Such valves may be used to prevent flow in one direction, as a non-limiting embodiment. The valve  1200  may be used in both the suction valves  100 S,  102 S and discharge valve  100 D,  102 D positions described in relation to  FIG. 8A  and  FIG. 8B . 
     Flow, Pressure and System Loading Benefits of Aspects of the Disclosure Compared with Conventional Apparatus 
     Prototypes of the arrangement  10  were constructed and tested. Operational parameters of conventional apparatus are compared to the arrangement  10  described above, illustrating the advance in performance. 
     Example Of Conventional Apparatus 
     Single acting piston system
 
Piston size—4° diameter
 
     Stroke—8″ 
     Rod loading maximum—250 000 lb f 
     Operating Speed—250 rpm 
     
       
         
           
             
               
                 
                   
                     Piston 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     area 
                   
                   = 
                     
                   ⁢ 
                   
                     π 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       
                         d 
                         2 
                       
                       / 
                       4 
                     
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     π 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       
                         4 
                         2 
                       
                       / 
                       4 
                     
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     12.57 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ins 
                       2 
                     
                   
                 
               
             
           
         
       
     
     Given a maximum rod load of 250 000 lb f, then the maximum pressure which be obtained would be:— 
     
       
         
           
             
               
                 
                   Pressure 
                   = 
                     
                   ⁢ 
                   
                     Force 
                     / 
                     Area 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     250 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       000 
                       / 
                       12.57 
                     
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     19 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     889 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     psi 
                   
                 
               
             
           
         
       
       
         
           
             
               
                 
                   
                     Flow 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     Volume 
                   
                   = 
                     
                   ⁢ 
                   
                     area 
                     × 
                     stroke 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     12.57 
                     × 
                     8 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     100.56 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ins 
                       3 
                     
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ( 
                       
                         per 
                         ⁢ 
                         
                             
                         
                         ⁢ 
                         piston 
                       
                       ) 
                     
                   
                 
               
             
           
         
       
       
         
           
             
               At 
               ⁢ 
               
                   
               
               ⁢ 
               operating 
               ⁢ 
               
                   
               
               ⁢ 
               speed 
             
             = 
             
               250 
               ⁢ 
               
                   
               
               ⁢ 
               rpm 
             
           
         
       
       
         
           
             
               
                 
                   
                     Total 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     flow 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     volume 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ( 
                       
                         per 
                         ⁢ 
                         
                             
                         
                         ⁢ 
                         piston 
                       
                       ) 
                     
                   
                   = 
                     
                   ⁢ 
                   
                     250 
                     × 
                     100.56 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     25 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     140 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ins 
                       3 
                     
                   
                 
               
             
             
               
                 
                     
                   ⁢ 
                   
                     ( 
                     
                       108.8 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       US 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       Gallon 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       per 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       minute 
                     
                     ) 
                   
                 
               
             
           
         
       
     
     Embodiment of the Present Disclosure Example 
     Piston size—4′ diameter 
     Piston Shaft—1.5″ 
     Stroke—8′ 
     Rod loading maximum—250 000 lb f 
     Operating Speed—250 rpm 
     
       
         
           
             
               
                 
                   
                     Piston 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     area 
                   
                   = 
                     
                   ⁢ 
                   
                     π 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       
                         ( 
                         
                           
                             D 
                             2 
                           
                           - 
                           
                             d 
                             2 
                           
                         
                         ) 
                       
                       / 
                       4 
                     
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     
                       π 
                       ( 
                       
                           
                       
                       ⁢ 
                       
                         
                           4 
                           2 
                         
                         - 
                         
                           1.5 
                           2 
                         
                       
                       ) 
                     
                     / 
                     4 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     10.8 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ins 
                       2 
                     
                   
                 
               
             
           
         
       
       
         
           
             
               
                 
                   
                     Flow 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     Volume 
                   
                   = 
                     
                   ⁢ 
                   
                     area 
                     × 
                     stroke 
                   
                 
               
             
             
               
                 
                     
                   ⁢ 
                   
                     ( 
                     
                       2 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       strokes 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       per 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       GARTECH 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       development 
                     
                     ) 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     10.8 
                     × 
                     8 
                     × 
                     2 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     172.8 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ins 
                       3 
                     
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ( 
                       
                         per 
                         ⁢ 
                         
                             
                         
                         ⁢ 
                         piston 
                       
                       ) 
                     
                   
                 
               
             
           
         
       
       
         
           
             
               At 
               ⁢ 
               
                   
               
               ⁢ 
               operating 
               ⁢ 
               
                   
               
               ⁢ 
               speed 
             
             = 
             
               250 
               ⁢ 
               
                   
               
               ⁢ 
               rpm 
             
           
         
       
       
         
           
             
               
                 
                   
                     Total 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     flow 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     volume 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ( 
                       
                         per 
                         ⁢ 
                         
                             
                         
                         ⁢ 
                         piston 
                       
                       ) 
                     
                   
                   = 
                     
                   ⁢ 
                   
                     250 
                     × 
                     172.8 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     43 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     200 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     
                       ins 
                       3 
                     
                   
                 
               
             
             
               
                 
                     
                   ⁢ 
                   
                     ( 
                     
                       187.2 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       US 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       Gallon 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       per 
                       ⁢ 
                       
                           
                       
                       ⁢ 
                       minute 
                     
                     ) 
                   
                 
               
             
           
         
       
     
     Pressure—if we take the limiting factor as pressure from above (19 889 psi), then the equivalent rod load would be 
       Pressure=Force/Area 
     Transposing 
     
       
         
           
             
               
                 
                   Force 
                   = 
                     
                   ⁢ 
                   
                     Pressure 
                     × 
                     Area 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     19 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     889 
                     × 
                     10.8 
                   
                 
               
             
             
               
                 
                   = 
                     
                   ⁢ 
                   
                     24 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     801 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     lb 
                     ⁢ 
                     
                         
                     
                     ⁢ 
                     f 
                   
                 
               
             
           
         
       
     
     Summary—Comparing the flow, pressure, and load values 
     Single Acting 
     Flow=108.8 gpm (per piston) 
     Pressure=19 889 psi 
     Rod Load=250 000 lb f 
     Double Acting 
     Flow=187.0 gpm (per piston) 
     Pressure=19 889 psi 
     Rod Load=214 801 lb f 
     Thus, aspects of the disclosure provide a roughly 72% increase in flow compared to conventional apparatus. 
     Aspects of the disclosure provide a pressure generating capacity—19 889 psi. 
     Aspects of the disclosure reduce equivalent rod load by nearly 15%. 
     Aspects described provide a scalable design, where the number of pistons can be altered to suit operator requirements, while maintaining the operational benefits, i.e. 3 piston, 5 piston, 7 piston . . . etc., configurations. 
     In one embodiment, the 7-piston configuration illustrated, is of a comparable size and weight to a convention 3 piston (Triplex) mud pump. However, the performance of the pump vastly increases the flow and thus other embodiments are possible. 
     SUMMARY OF BENEFITS OVER CONVENTIONAL APPARATUS 
     Aspects of the disclosure provide a configurable and scalable design to match operator requirements. 
     Aspects of the disclosure provide a similar weight and footprint to conventional pumps, while having an increased fluid volume discharge. 
     Aspects of the disclosure provide for a more efficient double acting flow/discharge. 
     Aspects of the disclosure provide a check valve design to minimize turbulent flow within the entire design. 
     Aspects of the disclosure provide a simple cartridge design for valves, allowing for easy maintenance and long service life. 
     Aspects of the disclosure provide a more simple and robust configuration that provides superior maintenance capability. 
     Aspects of the disclosure provide a modular construction that has the capability of being easily manufactured. 
     Aspects of the disclosure also provide for:
         1. Elimination of the crank shaft and associated components via two rotating parallel discs operating on the same axis thereby eliminating wear and failure points.   2. Replacement of a single acting piston or plunger with a double acting piston thereby increasing the output pumping volume, reducing the rod load, which increases pump life and safety.   3. Increasing the number of cylinder available to any odd number 3, 5, 7, 9, etc. thereby the pumps double acting capacity is further increased by a number of cylinders greater than 5.   4. Replacing single suction and discharge valves, with cartridge style dual suction and discharge valves, thereby facilitating the double acting piston or plunger and increasing valve life via the cartridge valve.       

     In one example embodiment, an arrangement is disclosed. The arrangement may comprise a shaft and two parallel tapered rotating discs bearing mounted on the shaft, such discs configured to rotate with the shaft, wherein a first portion of a first of the two parallel tapered rotating discs maintains a fixed distance between a corresponding second portion of a second of the two parallel tapered rotating discs during rotation of both of the two parallel tapered rotating discs with the shaft. The arrangement may also comprise at least one block arranged in a radial pattern between the two parallel tapered rotating discs; each of the at least one blocks having at least one void in each block. The arrangement may also comprise a piston located within the at least one void in the block, the piston configured to translate from a first position to a second position, between the tapered rotating discs. The arrangement may also comprise a first housing connected to the block, the first housing having a suction side and a discharge side, the first housing configured to channel a fluid. The arrangement may also comprise a second housing connected to the block, the second housing having a suction and a discharge side, the second housing configured to channel the fluid. The arrangement may also comprise at least a first suction check valve and a first discharge check valve located in the first housing. The arrangement may also comprise at least a second suction check valve and a second discharge check valve located in the second housing. 
     In another example embodiment, the arrangement may be configured wherein the translation of the piston from the first position to the second position occurs through actuation of a mechanical connection. 
     In another example embodiment, the arrangement may be configured wherein the mechanical connection is arranged so a first end of the piston is connected to a first of the rotating tapered discs and a second end of the piston is connected to a second of the rotating tapered discs. 
     In another example embodiment, the arrangement may be configured wherein the first housing is connected to the block through a first bolted connection. 
     In another example embodiment, the arrangement may be configured wherein the second housing is connected to the block through a second bolted connection. 
     In another example embodiment, the arrangement may be configured wherein each of the suction check valves is in a cartridge configuration. 
     In another example embodiment, the arrangement may be configured wherein each of the discharge check valves is in a cartridge configuration. 
     In another example embodiment, a method is disclosed. The method may comprise providing a fluid stream to a pump with two rotating tapered discs configured to rotate with a shaft and directing the fluid stream to at least one block having a piston. The method may also comprise rotating each of the two rotating tapered discs with the shaft, causing the at least one piston to translate with the at least one block, such translation creating both a suction and a compression within the block during the translation and moving the fluid stream in the at least one block during each compression stroke of the piston. 
     In another example embodiment, the method may be performed, wherein the fluid stream is a drilling mud. 
     In another example embodiment, the method may be performed, wherein the rotating of each of the two rotating tapered discs is at least 200 revolutions per minute. 
     In another example embodiment, the method may be performed, wherein the rotating of each of the two rotating tapered discs is approximately 250 revolutions per minute. 
     In another example embodiment, the method may be performed, wherein the moving the fluid stream in the at least one block during each compression stroke of the piston occurs in two directions of the piston. 
     In another example embodiment, the method may be performed, wherein the providing the fluid stream to the pump with two rotating tapered discs configured to rotate with a shaft is controlled by a fluid feeding system. 
     In another example embodiment, the method may be performed, wherein the fluid feeding system is computer controlled to feed a predetermined amount of fluid to the pump.