Synthesis of chiral amino cyclic phosphoric acids
Chiral amino cyclic phosphoric acids, 5-amino-2-hydroxy-4-(4-nitrophenyl)-1,3,2-dioxaphosphorinane 2-oxide and 2-hydroxy-4-(4-methylsulfonylphenyl)-5-phthalimido-1,3,2-dioxaphos phorinane 2-oxide are synthesized in good over yields (64.2% and 72.8% respectively) from 2-amino-1-aryl-1,3-propanediols. The different reaction conditions are necessary in hydrolysis reactions of amino cyclic phosphonyl chlorides.
Detection and characterization of ceramide-1-phosphate phosphatase activity in rat liver plasma membrane.
A calcium-dependent ceramide (Cer) kinase was recently detected in human leukemia (HL-60) cells (Kolesnick, R.N., and Hemer, M.R. (1990) J. Biol. Chem. 265, 18803-18808) where it may function in terminating the regulatory effects of Cer, and in synaptic vesicles (Bajjalieh, S. M., Martin, T. F. J., and Floor, E. (1989) J. Biol. Chem. 264, 14354-14360). We now demonstrate that the addition of both Cer-1-phosphate (Cer-1-P) and a short-acyl chain analog of Cer-1-P,N-hexanoylsphingosine-1-phosphate (C6-Cer-1-P) to cultured cells and a variety of subcellular fractions results in rapid degradation to Cer and C6-Cer, respectively. The Cer-1-P phosphatase activity is enriched in a rat liver plasma membrane fraction and appears to be distinct from the phosphatase that hydrolyzes phosphatidic acid (PA), PA phosphohydrolase, as shown by the difference in sensitivity of Cer-1-P and PA hydrolysis to propranolol, detergent, and heat treatment. Moreover, the Km of Cer-1-P hydrolysis is 10-fold lower than the Km of PA hydrolysis in plasma membrane. PA is a noncompetitive inhibitor of Cer-1-P hydrolysis, with an inhibition constant 1-1.5-fold higher than the Km of Cer-1-P hydrolysis. In contrast, Cer-1-P does not inhibit PA hydrolysis. Finally, we describe the synthesis of a novel analog of Cer-1-P which is not hydrolyzed in vitro and in vivo and is internalized in cultured cells by endocytosis. These results are discussed in relation to the possible roles of Cer-1-P in regulating intracellular levels of Cer.
Influence of pressure and fluidization velocity on the hydrodynamics of a fluidized bed containing horizontal tubes
Abstract An experimental investigation of the influence of horizontal tubes on the bubble behaviour and through-flow velocity of gas inside bubbles was carried out and the influence of pressure and fluidization velocity was studied. The visible bubble flow rate and the gas velocity through the bubbles were measured simultaneously in a pressurized fluidized bed, using capacitance and Pitot-static pressures probes respectively. Silica sand with a mean particle diameter of 0.7 mm was fluidized at pressures between 01. and 1.6 MPa, in a bed of 0.2 × 0.3 m cross-section. Six different horizontal tube configurations were used and comparisons were made with results obtained in the same bed operated without tubes. The results from the bed with tubes show that the influence of pressure and fluidization velocity is basically the same as in the bed without tubes; an increase in pressure and fluidization velocity increases the bubble activity. At low excess gas velocities, the influence of immersed tubes on the bubble behaviour is less pronounced than at high excess gas velocities. Measurements and visual observations show that a small tube pitch gives a more uniform distribution of the visible bubble flow over the bed cross-section. At a combination of high pressure, high excess gas velocity and a large tube pitch, a preferred bubble path was observed in the centre of the bed cross-section. The pressure probe measurements show that the through-flow velocity of gas inside the bubbles is in most cases higher when tubes are present in the bed. The through-flow velocity consistently decreases with increasing pressure in the bed without tubes. The tendency is largely the same at a low excess gas velocity when tubes are present, but at a high excess gas velocity the through-flow velocity first decreases and then increases as the pressure is increased.