Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Off-rates

A web of molten plastic is pulled from the die into the nip between the top and middle roUs. At the nip, there is a very small rolling bank of melt. Pressure between the roUs is adjusted to produce sheet of the proper thickness and surface appearance. The necessary amount of pressure depends on the viscosity. For a given width, thickness depends on the balance between extmder output rate and the take-off rate of the pull roUs. A change in either the extmder screw speed or the puU-roU speed affects thickness. A constant thickness across the sheet requires a constant thickness of melt from the die. The die is equipped with bolts for adjusting the die-gap opening and with an adjustable choker bar or dam located inside the die a few centimeters behind the die opening. The choker bar restricts flow in the center of the die, helping to maintain a uniform flow rate across the entire die width. [Pg.140]

In the tubular process a thin tube is extruded (usually in a vertically upward direction) and by blowing air through the die head the tube is inflated into a thin bubble. This is cooled, flattened out and wound up. The ratio of bubble diameter to die diameter is known as the blow-up ratio, the ratio of the haul-off rate to the natural extrusion rate is referred to as the draw-down ratio and the distance between the die and the frost line (when the extrudate becomes solidified and which can often be seen by the appearance of haziness), the freeze-line distance. [Pg.235]

In the event of faults developing (as indicated by high boil-off rates or external frost), cease using the equipment. [Pg.260]

Take-off rate from reflux drum (high)... [Pg.90]

Angle drop-off Rate of change (°/100 ft) of the inclination angle in the section of the wellbore that is decreasing toward vertical. [Pg.1079]

The Environmental Protection Agency (EPA) and other federal, state and local authorities govern security of supply in relation to quantity for surface and groundwater by the granting of an abstraction license. The license limits the total daily quantity and the rate at which the waters may be abstracted, taking account of the natural resource and the needs of other abstractors. Metered water supply is subject to contract with the water companies, who may impose quantity and draw-off rate limitations. The limitations imposed by the license or contract may influence plant location. [Pg.37]

K = 63 M 1, Kb = 1.4M-1)47 lithium-7 (K = 14 M 1 K" = 0.5 M 1) 49) and for cesium-133 (K, st 50 M-1, K = 4M 1)S0). In the case of sodium-23, transverse relaxation times could also be utilized to determine off-rate constants k ff = 3 x 105/sec k"ff = 2x 107/sec47,51). Therefore for sodium ion four of the five rate constants have been independently determined. What has not been obtained for sodium ion is the rate constant for the central barrier, kcb. By means of dielectric relaxation studies a rate constant considered to be for passage over the central barrier, i.e. for jumping between sites, has been determined for Tl+ to be approximately 4 x 106/sec 52). If we make the assumption that the binding process functions as a normalization of free energies, recognize that the contribution of the lipid to the central barrier is independent of the ion and note that the channel is quite uniform, then it is reasonable to utilize the value of 4x 106/sec for the sodium ion. [Pg.192]

A. Two site model with two equivalent non-interacting binding sites. Kb = 1.2 M 1, koff = 6.6x10 7 sec, kcb = 1.3 x 107/sec. This model is incorrect because a tight and a weak site have been observed with different off-rate constants as listed in part B. [Pg.193]

A fluid loss additive is described [1849] that helps achieve a desired fracture geometry by lowering the spurt loss and leak-off rate of the fracturing fluid into the surrounding formation by rapidly forming a filter-cake with low permeability. The fluid loss additive is readily degraded after the completion... [Pg.41]

Water-soluble organic polymers, sueh as hydroxethylcellulose, have been used to slow the leak-off rate of clear brines into permeable formations. Fluid loss or leak-off, however, can be effectively controlled only by bridging the pore openings with rigid or semirigid particles of sufficient size and number. [Pg.121]

Lee CK, Wang YM, Huang LS, Lin SM. 2007. Atomic force microscopy Determination of unbinding force, off rate and energy barrier for protein-ligand interaction. Micron 38 446-461. [Pg.632]

HTS data and secondary screening for hit validation and determination of kinetic on/off rates. These data have been successfully incorporated into hit triage by enhancing the understanding of SAR differences between potential scaffolds [24]. In this example, those differences allowed informed decision making in the choice of which series to pursue and which to deprioritize. [Pg.150]

Potential Clincial Advantages of Slow Off-rate Inhibitors... [Pg.153]

In the top (clarifying) zone the relatively clear liquid moves upward and overflows the top. In the middle zone the solid particles settle as the displaced liquid moves upward, and both the local solids concentration and the settling velocity vary from point to point. In the bottom (compressed) zone, the solids and liquid both move downward at a rate that is determined mainly by the underflow draw-off rate. For a given feed rate and solids... [Pg.431]

Because the batch flux data are obtained in a closed system with no outflow, the net solids flux is zero in the batch system and Eq. (14-40) reduces to FL = —(pV%/ 1 — cp). Note that FL and Vs are of opposite sign, because the displaced liquid moves upward as the solids settle. The relative velocity between the solids and liquid is Vr = Vs — VL which, from Eq. (14-20), is Vr = Fs/(1 — relative velocity that controls the dynamics in the thickener. If the underflow draw-off rate from the thickener is gu, the additional solids flux in the thickener due to superimposition of this underflow is qu = Qu/A = Vu. Thus, the total solids flux at any point in the thickener (qs) is equal to the settling flux relative to the suspension (i.e., the batch flux qsb) at that point, plus the bulk flux due... [Pg.434]


See other pages where Off-rates is mentioned: [Pg.455]    [Pg.320]    [Pg.461]    [Pg.20]    [Pg.460]    [Pg.258]    [Pg.191]    [Pg.231]    [Pg.269]    [Pg.312]    [Pg.37]    [Pg.39]    [Pg.56]    [Pg.231]    [Pg.71]    [Pg.122]    [Pg.68]    [Pg.132]    [Pg.186]    [Pg.153]    [Pg.208]    [Pg.216]    [Pg.229]    [Pg.226]    [Pg.204]    [Pg.432]    [Pg.435]    [Pg.435]   
See also in sourсe #XX -- [ Pg.21 , Pg.253 ]




SEARCH



Boil-off rate

Energy Balance Between Heat In-leaks and Boil-off Rates

Kinetics off-rate

Rate coefficients in the intermediate fall-off range

Rate ofFe

Rate ofFe

© 2024 chempedia.info