scholarly journals FERTILIZATION AND THE TEMPERATURE COEFFICIENTS OF OXYGEN CONSUMPTION IN EGGS OF ARBACIA PUNCTULATA

1934 ◽  
Vol 17 (5) ◽  
pp. 677-685 ◽  
Author(s):  
B. B. Rubenstein ◽  
R. W. Gerard

The eggs of A. punctulata have a high temperature coefficient in the resting state: Q10 = 4.1. On fertilization and on cytolysis the temperature coefficient falls to less than half the resting value: Q10 = 1.8 and 1.9 respectively. The factor by which oxygen consumption increases on fertilization is a variable, its magnitude depending on temperature as well as on egg species. It is nearly ten times greater at 11°C. and only double at 29.9°C. By extrapolating to 32°C. there would be no increase on fertilization. Critical thermal increments common to many oxidations, 6,500, 10,800, and 12,500, have been found. The possible significance of these results is discussed in relation to the catalytic mechanisms and structural organization of the egg cell.

2010 ◽  
Vol 97 (22) ◽  
pp. 223507 ◽  
Author(s):  
H. H. Radamson ◽  
M. Kolahdouz ◽  
S. Shayestehaminzadeh ◽  
A. Afshar Farniya ◽  
S. Wissmar

1984 ◽  
Vol 2 (5) ◽  
pp. 380-395 ◽  
Author(s):  
W.J. Parker

The calculation of heat release rate by oxygen consumption is based on the assumption that all materials release approximately the same amount of heat per unit mass of oxygen consumed. This technique is now being employed to determine the heat release rate of materials in various heat release rate cal orimeters. Other uses include the heat release rate of assemblies in the fire en durance furnaces and the total heat release rate in room fire tests. These dif ferent applications lead to different experimental procedures which require dif ferent formulas. The experimental choices or constraints include open or closed systems, paramagnetic or high temperature oxygen analyzers, CO2 analyzers or CO2 traps, and the use of a gas burner whose heat release rate must be deducted from the total. Various assumptions about CO levels in the exhaust duct and vitiation and humidity in the incoming air are made. General formulas for the heat release rate by oxygen consumption are developed in this paper from which the formulas for specific applications can easily be derived.


2019 ◽  
Vol 45 (2) ◽  
pp. 2185-2193 ◽  
Author(s):  
Liang Yan ◽  
Qiuyun Fu ◽  
Dongxiang Zhou ◽  
Mei Wang ◽  
Hao Zu ◽  
...  

2013 ◽  
Vol 2013 (HITEN) ◽  
pp. 000096-000103
Author(s):  
Yoann Dusé ◽  
Fabien Laplace ◽  
Nicolas Joubert ◽  
Xavier Montmayeur ◽  
Noureddine Zitouni ◽  
...  

We present in this paper two new products for high-temperature, low-voltage (2.8V to 5.5V) power management applications. The first product is an original implementation of a monolithic low dropout regulator (XTR70010), able to deliver up to 1A at 230°C with less than 1V of dropout. This new voltage regulator can source an output current level up to 1.5A. The regulated output voltage can be selected among 32 preset values from 0.5V to 3.6V in steps of 100mV, or it can be obtained with a pair of external resistors. The circuit integrates complex analog and digital control blocks providing state of the art features such as UVLO protection, chip enable control, soft start-up and soft shut-down, hiccup short-circuit protection, customer selectable thermal shut-down, input power supply protection, output overshoot remover and stability over an extremely wide range of load capacitances. The circuit offers a fair ±2% absolute accuracy and is guaranteed latch-up free. The second product is an advanced high-temperature, low-power, digitally trimmable voltage reference (XTR75020). Thanks to a custom, 1-wire serial interface, the absolute precision and the temperature coefficient can be adjusted in order to obtain an accuracy better than 0.5% with a temperature coefficient bellow ±20ppm/°C. On-chip OTP memory for trimming of absolute value and temperature coefficient makes the circuit extremely accurate and almost insensitive to drifts over time and temperature. The circuit features a class AB output buffer able to source or sink up to 5mA and remains stable with any load capacitance up to 50μF. The XTR75020 has nine preset possible output voltages. The source and sink short circuit current always remains bellow 25mA. The quiescent current consumption is 300μA typical at 230°C while the standby current is, in all cases, under 20μA. Both devices are designed on a latch-up free silicon-on-insulator process.


1976 ◽  
Vol 59 (5) ◽  
pp. 1188-1189
Author(s):  
Charles E Lewis ◽  
Martin G Croft

Abstract In using the Hanus method for determining the iodine absorption number of backfat from pigs, the blank determinations varied noticeably. Slight variations in temperature changed the volume of iodine solution dispensed, because the solvent, acetic acid, has a high temperature coefficient of expansion. For accurate, precise, and rapid determinations, the iodine solution should be measured by weight, not volume. Further modifications include the use of a stabilized indicator and a change in the dispensing of the weighed samples.


SPE Journal ◽  
2011 ◽  
Vol 16 (03) ◽  
pp. 513-523 ◽  
Author(s):  
A.A.. A. Mailybaev ◽  
J.. Bruining ◽  
D.. Marchesin

Summary There is a renewed interest in using combustion to recover medium- or high-viscosity oil. Despite numerous experimental, numerical, and analytical studies, the mechanisms for incomplete fuel combustion or oxygen consumption are not fully understood. Incomplete oxygen consumption may lead to low-temperature oxidation reactions downstream. This paper shows that these features emerge in a relatively simple 1D model, where air is injected in a porous medium filled with inert gas, water, and an oil mixture consisting of precoke, medium oil, and light oil. Precoke is a component that is dissolved in the oil but has essentially the same composition as coke. At high temperatures, precoke is converted to coke, which participates in high-temperature oxidation. At high temperatures, medium-oil components are cracked, releasing gaseous oil. Light-oil components and water are vaporized. The model possesses an analytical solution, which was obtained by a concept introduced by Zeldovich et al. (1985). This concept, which underlies most analytical approaches such as the reaction-sheet approximation and large-activation-energy asymptotics, entails that reaction can occur only in a very small temperature range because of the highly nonlinear nature of the Arrhenius factor. For a temperature below this range, the reaction rate is too slow, and for temperatures above this range, the reaction rate is so fast that either the fuel or oxygen concentrations become zero. The model results, in the absence of external heat losses, show that there are two combustion regimes in which coke or oxygen is partially consumed. In one regime, the reaction zone moves in front of the heat wave; whereas, in the other regime, the order of the waves is reversed. There are also two combustion regimes in which the coke and oxygen are completely consumed. Also, here the reaction zone can move in front of or at the back of the heat wave. Each combustion regime is described by a sequence of waves; we derive formulas for parameters in these waves. We analyze our formulas for typical in-situ-combustion data and compare the results with numerical simulation. The main conclusion is that mainly two key parameters (i.e., the injected oxygen mole fraction and the fuel concentration) determine the combustion-front structure and when either incomplete oxygen consumption or incomplete fuel consumption occurs in the high-temperature oxidation zone.


1951 ◽  
Vol 49 (2-3) ◽  
pp. 169-174 ◽  
Author(s):  
J. Gordon ◽  
R. A. Hall ◽  
L. H. Stickland

The lysis of Bacterium coli suspensions brought about by glycine shows the following characteristics:(1) There is a latent period of 2 hr., followed by a rapid lysis reaching a maximum in about 8 hr.(2) The extent of the lysis is independent of the dilution of the bacterial suspension over a wide range.(3) The extent of the lysis increases with the glycine concentration up to 10M, but is approaching a limit at this concentration.(4) The lysis is negligible below pH 5 and above pH 10, and shows a maximum rate in the region of pH 6–5–8–5.(5) The rate of lysis has a very high temperature coefficient (Q10 of the order of 5).


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