Operator, organizational, direct and general support maintenance manual : tank and pump unit, liquid dispensing for truck mounting (Highland Industries model 2000), FSN 4930-877-8678.

Includes index.

Organizational, direct, and general support maintenance repair parts and special tools list : tank and pump unit, liquid dispensing, for truck mounting (Highland Industries model 2000) FSN 4930-877-8678.

"April 1970."

Operator, organizational, direct support, and general support maintenance manual : tank and pump unit, liquid dispensing, for truck mounting (Advanced Industries model 1800) FSN 4930-070-1181.

"August 1972."

Operator, organizational, DS, and GS maintenance manual : generator set, diesel engine driven, liquid cooled, AC, 100 KW, 120 208, 240 416 volt, 3 phase, 4 wire, 50 60 HZ, skid mtd (Jeta power model D8001M) FSN 6115-156-4342).

"July 1970."

Crane-shovel : power unit, revolving truck mounted, pneumatic tired, 6x6, two engine drive, gasoline driven, 10 ton, 1/2 cu. yd. Bay City model 150M (less engines).

"March 1958."

Operator, organizational, direct and general support : pumping assembly, flammable liquid, bulk transfer, 50 GPM, (Barnes model 9117CA) Army model SPE 16 FSN 4320-728-0265, (Barnes model 15671CA)[ Army model SPE 16A FSN 4320-658-2888, (Barnes model 4074CA) FSN 4320-271-1858.

"May 1968."

Organizational and direct support maintenance repair parts and special tools lists : tank and pump unit, liquid dispensing, for truck mounting (United Manufacturing and Engineering Corp. model style 1), NSN 4930-00-542-2800 (model 2519) ... Altech Inc. model 4000), NSN 4930-00-926-3581.

"15 May 1980."

Operator's, organizational, and direct support maintenance manual: tank and pump unit, liquid dispensing, for truck mounting (United Manufacturing and Engineering Corp. model style 1), NSN 4930-00-542-2800 (model 2519) ... (Altech Inc. model 4000), NSN 4930-00-926-3581.

"31 July 1980."

Operator, organizational, and direct support maintenance manual including repair parts and special tools lists : heaters, space, radiant type, portable (type I, model M1941, solid fuel) FSN 4520-257-4877, (type II, model M1941, liquid fuel) FSN 4520-927-4214, (Yukon model M1950, solid or liquid fuel) FSN 4520-287-3353 : heaters, immersion, liquid fuel fired, for corrugated cans ....

"December 1969."

Operation and organizational maintenance manual : pumping assembly, flammable liquid, bulk transfer, gasoline engine driven, 350 gpm capacity, 275 feet total dynamic head, wheel mounted (Peabody Barnes, Inc. model US37ACG), FSN 4320-195-4914.

"January 1974."

A cold model study of raceway hysteresis

The effect of a gas flow field on the size of raceway has been studied experimentally using a two-dimensional (2-D) cold model. It is observed that as the blast velocity from the tuyere increases, raceway size increases, and when the blast velocity is decreased from its highest value, raceway size does not change much until the velocity reaches a critical velocity. Below the critical velocity, raceway size decreases with decreasing velocity but is always larger than that for the same velocity when the velocity increased. This phenomenon is called raceway hysteresis. Raceway hysteresis has been studied in the presence of different gas flow rates and different particle densities. Raceway hysteresis has been observed in all the experiments. The effect of liquid flow, with various superficial velocities, on raceway hysteresis has also been studied. A study of raceway size hysteresis shows that interparticle and particle-wall friction have a very large effect on raceway size. A hypothesis has been proposed to describe the hysteresis phenomenon in the packed beds. The relevance of hysteresis to blast furnace raceways has been discussed. Existing literature correlations for raceway size ignore the frictional effects. Therefore, their applicability to the ironmaking blast furnace is questionable.

Entanglement and spin squeezing in the two-atom Dicke model

We analyse the relation between the entanglement and spin-squeezing parameter in the two-atom Dicke model and identify the source of the discrepancy recently reported by Banerjee (2001 Preprint quant-ph/0110032) and Zhou et al (2002 J. Opt. B. Quantum Semiclass. Opt. 4 425), namely that one can observe entanglement without spin squeezing. Our calculations demonstrate that there are two criteria for entanglement, one associated with the two-photon coherences that create two-photon entangled states, and the other associated with populations of the collective states. We find that the spin-squeezing parameter correctly predicts entanglement in the two-atom Dicke system only if it is associated with two-photon entangled states, but fails to predict entanglement when it is associated with the entangled symmetric state. This explicitly identifies the source of the discrepancy and explains why the system can be entangled without spin squeezing. We illustrate these findings with three examples of the interaction of the system with thermal, classical squeezed vacuum, and quantum squeezed vacuum fields.

Parameters affecting the performance of wetting and drying in a two-dimensional finite element long wave hydrodynamic model

The marsh porosity method, a type of thin slot wetting and drying algorithm in a two-dimensional finite element long wave hydrodynamic model, is discussed and analyzed to assess model performance. Tests, including comparisons to simple examples and theoretical calculations, examine the effects of varying the marsh porosity parameters. The findings demonstrate that the wetting and drying concept of marsh porosity, often used in finite element hydrodynamic modeling, can behave in a more complex manner than initially expected.

A dynamic mathematical model for sequential leach bed anaerobic digestion of organic fraction of municipal solid waste

A mathematical model that describes the operation of a sequential leach bed process for anaerobic digestion of organic fraction of municipal solid waste (MSW) is developed and validated. This model assumes that ultimate mineralisation of the organic component of the waste occurs in three steps, namely solubilisation of particulate matter, fermentation to volatile organic acids (modelled as acetic acid) along with liberation of carbon dioxide and hydrogen, and methanogenesis from acetate and hydrogen. The model incorporates the ionic equilibrium equations arising due to dissolution of carbon dioxide, generation of alkalinity from breakdown of solids and dissociation of acetic acid. Rather than a charge balance, a mass balance on the hydronium and hydroxide ions is used to calculate pH. The flow of liquid through the bed is modelled as occurring through two zones-a permeable zone with high flushing rates and the other more stagnant. Some of the kinetic parameters for the biological processes were obtained from batch MSW digestion experiments. The parameters for flow model were obtained from residence time distribution studies conducted using tritium as a tracer. The model was validated using data from leach bed digestion experiments in which a leachate volume equal to 10% of the fresh waste bed volume was sequenced. The model was then tested, without altering any kinetic or flow parameters, by varying volume of leachate that is sequenced between the beds. Simulations for sequencing/recirculating 5 and 30% of the bed volume are presented and compared with experimental results. (C) 2002 Elsevier Science B.V. All rights reserved.

Permeability studies of alkylamides and caffeic acid conjugates from echinacea using a Caco-2 cell monolayer model

Background: Echinacea is composed of three major groups of compounds that are thought to be responsible for stimulation of the immune system-the caffeic acid conjugates, alkylamides and polysaccharides. This study has focussed on the former two classes, as these are the constituents found in ethanolic liquid extracts. Objective: To investigate the absorption of these two groups of compounds using Caco-2 monolayers, which are a model of the intestinal epithelial barrier. Results: The caffeic acid conjugates (caftaric acid, echinacoside and cichoric acid) permeated poorly through the Caco-2 monolayers although one potential metabolite, cinnamic acid, diffused readily with an apparent permeability (P-app) of 1x10(-4) cm/s. Alkylamides were found to diffuse through Caco-2 monolayers with P-app ranging from 3x10(-6) to 3x10(-4) cm/s. This diversity in P-app for the different alkylamides correlates to structural variations, with saturation and N-terminal methylation contributing to decreases in P-app. The transport of the alkylamides is not affected by the presence of other constituents and the results for synthetic alkylamides were in line with those for the alkylamides in the echinacea preparation. Conclusion: Alkylamides but not caffeic acid conjugates are likely to cross the intestinal barrier.