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Controllable fluid

Valve Application Technology Functional requirements and the properties of the controlled fluid determine which valve and actuator types are best for a specific apphcation. If demands are modest and no unique valve features are required, the valve-design style selection may be determined solely by cost. If so, general-purpose globe or angle valves provide exceptional value, especially in sizes less than 3-inch NFS and hence are very popular. Beyond type selection, there are many other valve specifications that must be determined properly in order to ultimately yield-improved process control. [Pg.787]

Figure 8.7(a) Variable-speed scoop control fluid coupling (Courtesy Fluidomat)... [Pg.201]

Control fluid quality during use, involving checks on correct dilution and make-up, concentration and freedom from contamination in service, regular cleaning and fluid changing Provide and use appropriate personal protective equipment A high standard of personal hygiene... [Pg.137]

Pumps, compressors, turbines, drivers, and auxiliary machinery should be designed to provide reliable, rugged performance. Pump selection and performance depend on the capacity required and tlie nature of Uie fluids involved. Remotely controlled power switches and shutoff valves are necessary to control fluid flow during an emergency. The inlets for air compressors should be strategically located to prevent the intake of hazardous materials. [Pg.495]

Hydraulic fluid contamination may be described as any foreign material or substance whose presence in the fluid is capable of adversely affecting system performance or reliability. It may assume many different forms, including liquids, gases, and solid matter of various composition, sizes, and shapes. Solid matter is the type most often found in hydraulic systems and is generally referred to as particulate contamination. Contamination is always present to some degree, even in new, unused fluid, but must be kept below a level that will adversely affect system operation. Hydraulic contamination control consists of requirements, techniques, and practices necessary to minimize and control fluid contamination. [Pg.602]

A valve is defined as any device by which the flow of fluid may be started, stopped, regulated or directed by a movable part that opens or obstmcts passage of the fluid. Valves must be able to accurately control fluid flow, system pressure and to sequence the operation of all actuators within a hydraulic system. [Pg.612]

A perfect temperature-controlled heat-transfer surface is difficult to achieve, but it is closely simulated in practice by using a control fluid on one side of, for example, a metal tube. The tube wall should be thin and, ideally, the heat-transfer resistance comparatively large for the other fluid on the working side of the tube the latter surface is then effectively temperature-controlled and responds only to changes in the control fluid. [Pg.210]

Pyrex jacket. The test fluid, distilled water, flowed vertically upwards through the annulus, while inside the heated tube a control fluid flowed which was either water or nitrogen gas, depending on the tube temperature required. [Pg.211]

The temperature control fluid is a 20% solution of commercial antifreeze in water. The fluid reservoir is a 20-liter insulated reservoir the fluid is kept above 60°C. Fluid from the reservoir is pumped through an electric heater to the jacket the fluid is heated to maintain the electrolyte temperature at 90°C. [Pg.537]

A derivatized hydroxyethylcellulose polymer gel exhibited excellent fluid-loss control over a wide range of conditions in most common completion fluids. This particular grated gel was compatible with the formation material and caused little or no damage to original permeability [1341]. Detailed measurements of fluid loss, injection, and regained permeability were taken to determine the polymer particulate s effectiveness in controlling fluid loss and to assess its ease of removal. Hydroxyethylcellulose can be etherified or esterified with long chain alcohols or esters. An ether bond is more stable in aqueous solution than is an ester bond [96]. [Pg.40]

However, production engineers have been reluctant to use particle bridging because of the possibility of particle transport into the formation, resulting in formation damage and/or costly and often ineffective stimulation treatments. A particle bridging fluid has been developed that quickly and effectively controls fluid loss in a wide range of permeabilities and pore diameters [916]. [Pg.121]

Fluid loss limits the effectiveness of acid fracturing treatments. Therefore formulations to control fluid loss have been developed and characterized... [Pg.271]

F F Chang and M. Parlar. Method and composition for controlling fluid loss in high permeability hydrocarbon bearing formations. Patent US 5981447,1999. [Pg.370]

M. Johnson. Fluid systems for controlling fluid losses during hydrocarbon recovery operations. Patent EP 691454,1996. [Pg.409]

H. C. Lau. Laboratory development and field testing of succinoglycan as a fluid-loss-control fluid. SPE Drilling Completion, 9(4) 221-226, December 1994. [Pg.421]

R. G. Udarbe, K. Hancock-Grossi, and C. R. George. Method of and additive for controlling fluid loss from a drilling fluid. Patent US 6107256, 2000. [Pg.472]

D. J. White, B. A. Holms, and R. S. Hoover. Using a unique acid-fracturing fluid to control fluid loss improves stimulation results in carbonate formations. In Proceedings Volume, pages 601-610. SPE Permian Basin Oil Gas Recovery Conf (Midland, TX, 3/18-3/20), 1992. [Pg.476]

C. D. Williamson. Chemically modified lignin materials and their use in controlling fluid loss. Patent GB 2210888, 1989. [Pg.477]

Atrial natriuretic peptide (ANP), brain natriuretic peptide (BNP), and C-type natriuretic peptide (CNP) are members of a family of so-called natriuretic peptides, synthesized predominantly in the cardiac atrium, ventricle, and vascular endothelial cells, respectively (G13, Y2). ANP is a 28-amino-acid polypeptide hormone released into the circulation in response to atrial stretch (L3). ANP acts (Fig. 8) on the kidney to increase sodium excretion and glomerular filtration rate (GFR), to antagonize renal vasoconstriction, and to inhibit renin secretion (Ml). In the cardiovascular system, ANP antagonizes vasoconstriction and shifts fluid from the intravascular to the interstitial compartment (G14). In the adrenal cortex, ANP is a powerful inhibitor of aldosterone synthesis (E6, N3). At the hypothalamic level, ANP inhibits vasopressin secretion (S3). It has been shown that some of the effects of ANP are mediated via a newly discovered hormone, called adreno-medullin, controlling fluid and electrolyte homeostasis (S8). The diuretic and blood pressure-lowering effect of ANP may be partially due to adrenomedullin (V5). [Pg.99]

Schell, D. A., Vari, R. C., and Samson, W. K., Adrenomedullin A newly discovered hormone controlling fluid and electrolyte homeostasis. Trends Endocrinol. Metab. 7,7-13 (1996). [Pg.127]

In extreme situations, incompatibility between injection fluids and reservoir components can be so great that deep-well disposal will not be the most cost-effective approach to waste disposal. In other situations, such remedial measures as pretreatment or controlling fluid concentrations or temperatures can permit injection even when incompatibilities exist. In addition to operational problems, waste-reservoir incompatibility can cause wastes to migrate out of the injection zone (casing/confining-layer failure) and even cause surface-water contamination (well blowout). [Pg.813]

Controlling fluid loss loss is particularly important in the case of the expensive high density brine completion fluids. While copolymers and terpolymers of vinyl monomers such as sodium poly(2-acrylamido-2-methylpropanesulfonate-co-N,N-dimethylacrylamide-coacrylic acid) has been used (H)), hydroxyethyl cellulose is the most commonly used fluid loss additive (11). It is difficult to get most polymers to hydrate in these brines (which may contain less than 50% wt. water). The treatment of HEC particle surfaces with aldehydes such as glyoxal can delay hydration until the HEC particles are well dispersed (12). Slurries in low viscosity oils (13) and alcohols have been used to disperse HEC particles prior to their addition to high density brines. This and the use of hot brines has been found to aid HEC dissolution. Wetting agents such as sulfosuccinate diesters have been found to result in increased permeability in cores invaded by high density brines (14). [Pg.11]

Intermixing of the polymer mobility control fluid with the surfactant slug can result in surfactant - polymer interactions which have a significant effect on oil recovery (476). Of course, oil - surfactant interactions have a major effect on interfacial behavior and oil displacement efficiency. The effect of petroleum composition on oil solubilization by surfactants has been the subject of extensive study (477). [Pg.43]

The primary factor controlling how much gas is in the form of discontinuous bubbles is the lamellae stability. As lamellae rupture, the bubble size or texture increases. Indeed, if bubble coalescence is very rapid, then most all of the gas phase will be continuous and the effectiveness of foam as a mobility-control fluid will be lost. This paper addresses the fundamental mechanisms underlying foam stability in oil-free porous media. [Pg.461]

A notable aspect of this equation is that L appears within it as prominently as the rate constant k+ or the groundwater velocity vx, indicating the balance between the effects of reaction and transport depends on the scale at which it is observed. Transport might control fluid composition where unreacted water enters the aquifer, in the immediate vicinity of the inlet. The small scale of observation L would lead to a small Damkohler number, reflecting the lack of contact time there between fluid and aquifer. Observed in its entirety, on the other hand, the aquifer might be reaction controlled, if the fluid within it has sufficient time to react toward equilibrium. In this case, L and hence Da take on larger values than they do near the inlet. [Pg.306]

In patients with mild AP, pain control, fluid and electrolyte status, and nutrition should be assessed periodically depending on the degree of abdominal pain and fluid loss. [Pg.322]

Example 7.10. Prins et al. [306] used electrowetting to control fluid motion in microchannels. To do so, they coated aluminum electrodes first with a 12 pm thick layer of parylene and then with a 10 nm thick fluoropolymer film. The channels were 0.35 mm wide. Due to the hydrophobic polymer water does not flow into the capillaries. Only after applying voltages of typically 200 V did the capillaries fill with water. When switching the voltage off, the water flowed out of the capillaries again. [Pg.143]


See other pages where Controllable fluid is mentioned: [Pg.261]    [Pg.373]    [Pg.194]    [Pg.991]    [Pg.44]    [Pg.419]    [Pg.332]    [Pg.13]    [Pg.177]    [Pg.196]    [Pg.164]    [Pg.221]    [Pg.222]    [Pg.607]    [Pg.473]    [Pg.244]    [Pg.741]    [Pg.373]   
See also in sourсe #XX -- [ Pg.187 ]




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Aqueous fluid control materials

Control fluids

Control fluids

Control of a Fluid Catalytic Cracker

Control valves compressible fluids

Diffusion controlled reactions, supercritical fluids

Drilling fluids control

Drilling fluids control mechanisms

Drilling fluids solids control

Element mobility fluid controlled

Flow control fluids

Fluid Loss Control Additives

Fluid chromatograph, supercritical controlled flow

Fluid control panel

Fluid cracking conversion control

Fluid cracking operation control

Fluid flow control valve

Fluid loss control

Fluid loss control agents

Fluid product control

Fluid velocity control, column

Geology fluid control

High pressure fluids controls

Hydraulic fluids contamination control

Microfluidic devices, fluid control strategies

Mobility-control fluid

Pressure-programmed controlled-flow supercritical fluid

Speed control fluid couplings

Tectonic control on magmatic fluid location

Temperature control system fluid

Thermodynamics Process Control in Fluid-phase Equilibria

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