Nitrogen, Liquefied

Compound Name Hydrogen, Liquefied Camphor Oil Nitrogen, Liquefied Nitrogen Tetroxide Oxygen, Liquefied Oil Mineral Carbolic Oil Litharge... 

Composition Mixture of liquefied nitrogen dioxide with carbon disulfide or gasoline. 

Has not been obtained in a condition of purity. A mixture of 95 per cent of N O, with 5 per cent, of N O may, however, be obtained by decomposing liquefied nitrogen tetroxide with a small quantity of H O at a low temperature 4NO, + H,0 = 2HNO, -h This is a dark... 

A V-5 Safe Handling of Liquefied Nitrogen And Argon. Covers properties of cryogenic liquids, con-... 

AV-5 Safe Handling of Liquefied Nitrogen and Argon. Coverage includes properties of cryogenic liquids, containers, safety precautions, standard connections, materials compatibility, first aid, and hazards of oxygen-deficient atmospheres. In formats of videotape or 80 audio-sequenced slides. (23 05 minutes)... 

S nomm Nitrocarbol Nitrocellulose Gum Nitrocellulose Solution Nitrochloroform Nitroe thane Nitrogen Dioxide Nitrogen, Liquefied Nitrogen Monoxide Nitrogen Peroxide Nitrogen Tetroxide Nitromethane... 

The ideal work to liquefy nitrogen under these conditions from Example 4.2 is 768 kJ/kg. Equation (4.8) then can be used to determine the figure of merit ... 

Example 5.9. A simple Linde cycle is utilized to liquefy nitrogen and operates between 0.101 and 10.1 MPa. If the temperature of the high-pressure gas leaving the compressor is 300 K and the compressor operates isothermally and reversibly, what is... 

Consider the Claude refrigerator as shown in Fig. 4.12 and modify it to liquefy nitrogen. The compressor, which operates isothermally at 300 K between 0.101 and 3.03 MPa, is known to have an overall efficiency of 70%. Eighty percent of the gas is sent through the expander with an inlet temperature of 250 K. The thermodynamic and mechanical efficiencies of the expander are 80% and 90%, respectively. Determine the percent decrease in liquid yield and FOM that is experienced in this liquefier over one with compressor and expander efficiencies of 100%. Assume all heat exchangers have an effectiveness of 100%. 

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