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Hiflow ring metal

Hiflow Rings Metal, plastic Rauschert Industries... [Pg.736]

Figure S.3 (Continued) Third generation metal random packings, (g) Hiflow ring ... Figure S.3 (Continued) Third generation metal random packings, (g) Hiflow ring ...
When molasses is fermented to produce a liquor containing ethanol, a C02-rich vapor containing a small amount of ethanol is evolved. The alcohol will be recovered by countercurrent absorption with water in a packed-bed tower. The gas will enter the tower at a rate of 180 kmol/h, at 303 K and 110 kPa. The molar composition of the gas is 98% C02 and 2% ethanol. The required recovery of the alcohol is 97%. Pure liquid water at 303 K will enter the tower at the rate of 151.5 kmol/h, which is 50% above the minimum rate required for the specified recovery (Seader and Henley, 1998). The tower will be packed with 50-mm metal Hiflow rings and will be designed for a maximum pressure drop of 300 Pa/m of packed height. [Pg.237]

Now, we estimate the pressure drop for operation at 70% of flooding using the Billet and Schultes (1991a) correlation. From Table 4.1, for 50-mm metal Hiflow rings ... [Pg.240]

Consider the absorber of Examples 3.7 and 5.2. The adsorber will be packed with 50-mm metal Hiflow rings. Estimate the dimensions of the absorber and the power required to pump the gas and the liquid through the tower. Design for a gas-phase pressure drop of 300 Pa/m of packed height. [Pg.295]

Consider the ethanol absorber of Example 4.4, packed with 50-mm metal Hiflow rings. Estimate the packed height required to recover 97% of the alcohol, using pure water at a rate 50% above the minimum and with a gas-pressure drop of 300 Pa/m. The system ethanol-C02-water at the given temperature and pressure obeys Henry s... [Pg.299]

Air at 300 K is used to dry a plastic sheet. The solvent wetting the plastic is acetone. At the end of the dryer, the air leaves containing 2.0 mol% acetone. The acetone is to be recovered by absorption with water in a packed tower. The gas composition is to be reduced to 0.05 mol% acetone. The absorption will be isothermal because of cooling coils inside the tower. For the conditions of the absorber, the equilibrium relationship is y. = 1.8 c.. The rich gas enters the tower at a rate of 0.252 kg/s, and pure water enters the top at the rate of 0.34 kg/s. The tower is packed with 25-mm metal Hiflow rings. Determine the dimensions of the tower. [Pg.320]

Repeat Example 6.16 for a tower packed with 50-mm metal Hiflow rings. Design for a 70% approach to flooding. [Pg.395]

Hiflow rings, structured Sulzer gauze packings (type BX), as well as type X sheet metal packings and Montz packings X with flow channels of a = 30° resulted in a higher flooding point constant Cfi,o. compared to Eq. (2-64), namely ... [Pg.76]

Figure 2-25. Capacity diagram F v,f1 = f(XFi) for random 25—50 mm metal Hiflow rings... Figure 2-25. Capacity diagram F v,f1 = f(XFi) for random 25—50 mm metal Hiflow rings...
Billet R, Mackowiak J. Hiflow-Ring ein Hochleistungsfullkorper fur Gas-Fliissig-Systeme. Teil 2 Aus-fuhrung in Metall. Chemie-Technik, vol. 14 (1985) no. 4, p. 91/99... [Pg.119]


See other pages where Hiflow ring metal is mentioned: [Pg.1168]    [Pg.42]    [Pg.45]    [Pg.68]    [Pg.132]    [Pg.132]    [Pg.162]    [Pg.162]    [Pg.162]    [Pg.197]    [Pg.213]    [Pg.238]    [Pg.256]    [Pg.268]    [Pg.268]    [Pg.302]    [Pg.158]    [Pg.170]    [Pg.1168]    [Pg.42]    [Pg.45]    [Pg.68]    [Pg.132]    [Pg.132]    [Pg.162]    [Pg.162]    [Pg.162]    [Pg.197]    [Pg.213]    [Pg.238]    [Pg.256]    [Pg.268]    [Pg.268]    [Pg.302]    [Pg.158]    [Pg.170]    [Pg.430]    [Pg.227]    [Pg.228]    [Pg.234]    [Pg.236]    [Pg.239]    [Pg.242]    [Pg.430]    [Pg.15]    [Pg.22]    [Pg.42]    [Pg.43]    [Pg.60]    [Pg.64]    [Pg.73]    [Pg.84]    [Pg.87]    [Pg.133]    [Pg.143]    [Pg.144]    [Pg.145]   
See also in sourсe #XX -- [ Pg.288 ]




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