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K Storage

K Storage ol raw rnalerei L Electronic weighing scale VI Inlerrnediate bm... [Pg.760]

Vector Enei density [kWh/k >] Storage capacity [wt%] Working temperature [K] Enei needed for storage [%<2)] Transmission efficiency [%]... [Pg.162]

Processing and supporting long-term storage of moderator in Biulding lOS-K storage areas... [Pg.72]

Kotarba, A., Km, I. Sojka, Z. (2002). Energetics of potassium loss from styrene catalyst model components reassignment of K storage and release phases. J. Catal, 211, 265-272. [Pg.211]

Coley, T.R. (1989), Diesel fuel additives influencing flow and storage properties . In Gasoline and diesel fuel additives (Owen, K. Ed.). John Wiley. [Pg.454]

Direct SCF calculations [J. Almlof, K. Faegri Jr., and K. Korsell, J. Comp. Chem. 3, 385 (1982)] offer a solution to this problem by eliminating the storage of two-electron integrals. This can, however, only be done at the expense of having to recompute integrals for every iteration. [Pg.266]

Fig. 38. Caustic purification system a, 50% caustic feed tank b, 50% caustic feed pumps c, caustic feed preheater d, amonia feed pumps e, ammonia feed preheater f, extractor g, trim heater h, ammonia subcooler i, stripper condenser j, anhydrous ammonia storage tank k, primary flash tank 1, evaporator reboiler m, evaporator n, caustic product transfer pumps o, purified caustic product cooler p, purified caustic storage tank q, ammonia stripper r, purified caustic transfer pumps t, overheads condenser u, evaporator v, evaporator vacuum pump w, aqueous storage ammonia tank x, ammonia scmbber y, scmbber condenser 2, ammonia recirculating pump aa, ammonia recycle pump. CW stands for chilled water. Fig. 38. Caustic purification system a, 50% caustic feed tank b, 50% caustic feed pumps c, caustic feed preheater d, amonia feed pumps e, ammonia feed preheater f, extractor g, trim heater h, ammonia subcooler i, stripper condenser j, anhydrous ammonia storage tank k, primary flash tank 1, evaporator reboiler m, evaporator n, caustic product transfer pumps o, purified caustic product cooler p, purified caustic storage tank q, ammonia stripper r, purified caustic transfer pumps t, overheads condenser u, evaporator v, evaporator vacuum pump w, aqueous storage ammonia tank x, ammonia scmbber y, scmbber condenser 2, ammonia recirculating pump aa, ammonia recycle pump. CW stands for chilled water.
K. C. Hoffman and co-workers, "Metal Hydride Storage for MobUe and Stationary AppUcations," SAE Fuels andUubricants Meeting St. Louis, Mo., 1976. [Pg.463]

The writing process, that is, the transition crystalline — amorphous, is caused by briefly (<50 100 ns) heating up the selected storage area (diameter (( )) ca 0.5—1 Hm) by a laser pulse to a temperature above the melting point of the memory layer (Eig. 15, Record), such that the film locally melts. When cooled faster than a critical quench rate (10 -10 ° K/s), the formation of crystalline nuclei is suppressed and the melted area sohdifies into the amorphous (glass-like) state. [Pg.149]

R. S. Jones and J. E. Kuder, ia K. L. Mittal, ed., Proc. Amer. Chem. Soc. Symp. on Polymers in Information Storage Technology, Los Angeles, Calif., Sept. [Pg.164]

Volatile organic Uquid storage vessels, including petroleum Uquid storage vessels (Subparts K, Ka, and Kb)... [Pg.77]

With appropriate caUbration the complex characteristic impedance at each resonance frequency can be calculated and related to the complex shear modulus, G, of the solution. Extrapolations to 2ero concentration yield the intrinsic storage and loss moduH [G ] and [G"], respectively, which are molecular properties. In the viscosity range of 0.5-50 mPa-s, the instmment provides valuable experimental data on dilute solutions of random coil (291), branched (292), and rod-like (293) polymers. The upper limit for shearing frequency for the MLR is 800 H2. High frequency (20 to 500 K H2) viscoelastic properties can be measured with another instmment, the high frequency torsional rod apparatus (HFTRA) (294). [Pg.201]

K. R. BuUock, "The Development and AppHcations of Storage Batteries—Historical Perspectives and Future Prospects," in Proceedings, 7th Australian Electrochemistry Conference, 1988. [Pg.579]

K. K. Humphreys and D. R. Brown, Ufe Cycle Cost Comparison of Advanced Storage Batteries and Duel Cells for Utility Stand-Alone and Electric Uehicle Application, Pacific Northwest Laboratory, BatteUe Memorial Institute, 1990. [Pg.581]

K. L. Mittal, Polymers in Information Storage, Plenum Press, New York, 1989. [Pg.438]

I. Gottberg, E. Hogberg, and K. Weber, Sulfur Storage and Hydrogen Sulphide Release From a Three-Way Catalyst Equipped Car, SAE 890491, Society of Automotive Engineers, Warrendale, Pa., 1989. [Pg.496]


See other pages where K Storage is mentioned: [Pg.126]    [Pg.389]    [Pg.158]    [Pg.253]    [Pg.271]    [Pg.400]    [Pg.402]    [Pg.281]    [Pg.245]    [Pg.144]    [Pg.393]    [Pg.262]    [Pg.272]    [Pg.126]    [Pg.389]    [Pg.158]    [Pg.253]    [Pg.271]    [Pg.400]    [Pg.402]    [Pg.281]    [Pg.245]    [Pg.144]    [Pg.393]    [Pg.262]    [Pg.272]    [Pg.304]    [Pg.322]    [Pg.266]    [Pg.89]    [Pg.291]    [Pg.7]    [Pg.10]    [Pg.34]    [Pg.230]    [Pg.461]    [Pg.281]    [Pg.412]    [Pg.429]    [Pg.406]    [Pg.425]    [Pg.330]    [Pg.581]    [Pg.24]    [Pg.342]    [Pg.334]    [Pg.335]    [Pg.316]   
See also in sourсe #XX -- [ Pg.252 , Pg.260 ]




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K-Reactor Moderator Storage Areas

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