1. n. [Drilling]
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The primary and probably most important device on the rig for removing drilled solids from the mud. This vibrating sieve is simple in concept, but a bit more complicated to use efficiently. A wire-cloth screen vibrates while the drilling fluid flows on top of it. The liquid phase of the mud and solids smaller than the wire mesh pass through the screen, while larger solids are retained on the screen and eventually fall off the back of the device and are discarded. Obviously, smaller openings in the screen clean more solids from the whole mud, but there is a corresponding decrease in flow rate per unit area of wire cloth. Hence, the drilling crew should seek to run the screens (as the wire cloth is called), as fine as possible, without dumping whole mud off the back of the shaker. Where it was once common for drilling rigs to have only one or two shale shakers, modern high-efficiency rigs are often fitted with four or more shakers, thus giving more area of wire cloth to use, and giving the crew the flexibility to run increasingly fine screens.
Alternate Form: shaker
See: cuttings, desander
Today&#;s shale shakers must be capable of maintaining optimum fluid properties to maximize drilling efficiency.
Joe Bacho
Shale shakers are components of the solids control systems. Shale shaker mainly used in the oil and gas drilling industry. Shale shaker is the first phase of a solids control system on a drilling rig, and are used to remove large solids (cuttings) from the drilling fluid (&#;mud&#;).
Shaker screen selection has the largest impact on the overall performance of the shale shaker. It is therefore important to understand the factors which may impact screen performance and how to properly select screens. Shaker screen performance is measured by:
Linear motion shale shakers use two motors vibrate in-phase for separation. The structure of this type of shaker is simple, easy to maintain, and repair. Linear motion provides superior cuttings conveyance and is able to operate at an uphill slope to provide improved liquid retention.
The abrupt changes in acceleration during the vibration cycle tends to cause screens to wear more quickly unless close attention is paid to tensioning and screen support techniques. Perforated metal backing plates and pre-tensioned screen panels have been specifically developed to address this problem.
Linear motion shakers usually operate at less than 4.0 G&#;s (normal to the screen) to balance screen life with processing capacity. Regardless, the finer screens normally run on linear motion shakers cannot be expected to outlast the coarser screens used in the past. For screens finer than 100 mesh, expect an average service life in excess of 100 hours.
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A balanced elliptical motion shale shaker can effectively remove solids and eliminate larger particles in drilling fluids. The relatively moderate vibration strength of balanced elliptical shale shakers can reduce screen consumption. It performs perfectly while drilling top-hole sections where heavy, high-volume solids are present.
On a balanced elliptical shale shaker, the difference in power between the two vibrating motors results in an unbalanced force. The structure of this type of shaker is more complex than a linear motion shaker. The price is higher.
The smooth change in acceleration with respect to direction translates into longer screen life compared to other vibration patterns. However, many circular motion shakers were designed before the advent of fine mesh screens and may provide less support for the screens. This will tend to negate much of the screen life benefit associated with circular
motion.
The definition of &#;acceptable&#; screen life must be judged within the context of the total solids removal system economics. Besides screen replacement cost, consideration must be given to the costs of drilling mud dilution and waste disposal costs when determining whether longer screen life is warranted at the expense of solids removal efficiency. In
weighted mud applications, the economic benefits of improved solids removal efficiency usually outweigh the additional screen costs.
Only very general correlations may be made between screen composition and service life. Unfortunately, features that lead to improved life are usually detrimental to flow capacity. Using heavier wires with greater tensile strength or adding supporting layers of cloth can both reduce conductance.
Increasing support through an additional bonding area (smaller plate openings) eliminates the usable screening area. Also, support techniques and screen tension can have a major effect on on-screen life. As a result, screen panels are typically designed to balance flow capacity performance with screen life.
Screen life is heavily dependent upon flow line conditions. Solids loading rate drilled cuttings abrasiveness, and shaker dynamics can easily outweigh composition effects.
The separation performance of a shale shaker screen (or any other solids control device) is commonly represented by its percent separated, or grade efficiency, curve. This curve is generated from full-scale experimental measurements and depicts the percent solids
removed as a function of particle size.
It reports the screen&#;s probability of separating any specific particle size with a given shaker under conditions specific to the test. Grade efficiency is the preferred measure of separation performance because it is independent of feed particle size distribution.
An example of a percent-separated curve is shown in Fig. 1. In this example, the median size separated by the screen was 145 microns. This means that 50% of the solids with a diameter of 145 microns were removed. A rough estimate of the median cut point (d50) can be made in the field by the wet sieve procedure (see Field Procedure to Estimate
Cut Point).
THE SHALE SHAKER, CLEANING ELEMENT OF THE SYSTEM OF DRILLING MUD
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APR has developed a method to characterize the relative separation efficiency potential of shaker screens without the expense and time required for full-scale testing. The technique links the relative separation performance of screens to a volume-equivalent distribution of their opening sizes.
The screen&#;s openings are measured using PC-based image analysis technology. Each opening in the screen is then represented by a spherical diameter corresponding to an ellipsoidal volume calculated from the image analysis data.
The cumulative volume of these ellipsoids, when plotted as a function of spherical diameter, yields a curve that correlates well with the standard grade efficiency curve. This curve represents the &#;separation potential&#; of the screen. The word &#;potential&#; is used because the screen&#;s separation performance is not measured directly, but implied by the size of the screen&#;s apertures.
Note: Grade separation efficiencies as measured on the shaker are subject to specific shaker and flowline conditions. They may not always agree with separation potential values. For example, the separation potential value for a screen with rectangular openings may be
pessimistic when drilling clean sand sections producing predominantly spherical sand grains. The image analysis method assumes solids of all shapes and sizes are available to the screen. However, on average, the separation potential values have been shown to adequately represent the screen&#;s separation performance.
The concept of a mesh includes sorting and supporting mesh webs, supporting metal grids, frames, etc. Screens for vibrating sieves are made of different materials, as a result of which there is a big difference in both price and quality.
The size of the individual mesh cells is decisive for the separation process.
Typically, the markings indicate the number of cells per linear inch (25.4 mm) and referred to as the &#;mesh&#; number. Since both square and rectangular cells are offered, the mesh count is usually specified in the x and y directions. By the number of meshes, you can determine what kind of mesh fabric we are talking about, for example
The full mesh description, according to the API, also contains information about the cell width in microns, the wire diameter and the total cell area in microns. In addition, by the number of mesh, you can classify the type of solid phase, for example:
Shales and clays in solution (eg bentonite) refer to the colloidal phase with a particle size of less than 2 microns.
Square meshes are most commonly used in the reconstitution process. Rectangular meshes are used to avoid clogging. Compared to square grids, the area of &#;&#;the cells increases for rectangular grids. When the particle size coincides with the mesh size of the canvas, they are easier to sift through rectangular mesh.
The correct choice of meshes can be judged when 3/4 of the mesh on the vibrating screen is covered with drilling mud, and 1/4 is filled with separated drilled cuttings.
Webs with a small mesh size, or solutions with a high relative viscosity, cause clogging of the meshes. As a result, a liquid film forms on the cells, which impairs the free passage of the drilling fluid, which leads to a deterioration in the separation process. To reduce clogging of the cells, it is preferable to use multi-layer webs.
Please note that the API specification can only apply to single-ply mesh webs with the same wire diameter in both directions. For multi-layer canvases, this specification does not apply.
mongoose pyramid screenShale Shaker And How Select Proper One For Your Mud Separation Project
The liquid throughput capacity of a screen panel is primarily a function of screen conductance and usable area. Conductance describes the ease with which fluid can flow through a unit area of screen cloth. In simplistic terms, it is analogous to permeability with the length in the direction of flow (screen thickness) taken into account. Higher conductances will result in higher flow rates through the screen.
Conductance is calculated from the mesh count and wire diameters of the screen cloth by the equations given in Appendix B, Conductance Calculation. Multilayer screens can also be handled by the conductance equation. The inverse of conductance for each screen layer is summed to equal the inverse of the net overall conductance:
1/Ct=1/C1+1/C2&#;&#;&#;1/Cn
This is valid provided that the screen layers used in the composition are designed to remain in contact.
Hunter MG4 Shale ShakerOilfield screens are typically bonded to a perforated metal panel or plastic grid to provide extra strength and improve service life. This practice eliminates some of the usable areas through which fluid may pass. Some metal backing plate designs may reduce the effective
screening area by as much as 40 percent. Because conductance describes screen flow capacity per unit area, the usable unblocked area available for screening must also be considered when comparing the mud processing capacity of shaker screen panels.
Shale shaker design
During the operation of the shale shaker, you should pay attention to the following rules:
The performance of the shaker can be optimized according to several criteria:
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Drilling Cuttings(Solids) and Gas Removal Equipment In Mud Circulating System