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Packings Intalox saddles

Tower packing, Intalox saddles, 1 in. nominal size. ... [Pg.735]

Tower packing Intalox saddles, tellerette rings, and pall rings may be considered. [Pg.150]

Fig. 21. Random packing elements for distillation columns (a), Raschig ring (metal) (b). Bed saddle (ceramic) (c), Intalox saddle (ceramic) (d), PaH ring... Fig. 21. Random packing elements for distillation columns (a), Raschig ring (metal) (b). Bed saddle (ceramic) (c), Intalox saddle (ceramic) (d), PaH ring...
TABLE 23-6 Typical Values of Kgo for Absorption in Towers Packed with 1.5-in Intalox Saddles at 25% Completion of Reaction ... [Pg.2107]

The only available test data [44] indicate that the plain flat plate (26-45% free area) has a decided detrimental effect on the allowable flooding conditions of the tower whereas the wire screen, weir-type, and fused Raschig ring designs have very little effect when using Intalox saddles for packing. [Pg.312]

Bulletin S-29, Intalox Saddle Packing, The United States Stoneware Co., Akron, Ohio. [Pg.411]

Absorption column diameter 1 m, vessel overall height 15 m, packed height 12 m, packing 25 mm ceramic intalox saddles, vessel carbon steel, operating pressure 5 bar. [Pg.267]

Figure 11.37. Types of packing (Norton Co.), (a) Raschig rings (b) Pall rings (c) Berl saddle ceramic (d) Intalox saddle ceramic (e) Metal Hypac (/) Ceramic, super Intalox... Figure 11.37. Types of packing (Norton Co.), (a) Raschig rings (b) Pall rings (c) Berl saddle ceramic (d) Intalox saddle ceramic (e) Metal Hypac (/) Ceramic, super Intalox...
Intalox saddles, Super Intalox and Hypac packings are proprietary design, and registered trade marks of the Norton Chemical Process Products Ltd. [Pg.592]

The pilot scale experiments were carried out in a CD column 23 ft (7 m) tall with a total packing height of 16 ft (4.9 m) and a 1 (2.54 cm) nominal I.D. The column is made of 316 SS and consists of 5 sections that are connected by flanges. Two 2 ft (0.6 m) sections located above a 9 ft (2.7 m) stripping section and below a 3 ft (0.9 m) rectification section, were used as the reaction zones, which contained the catalyst. The non-reactive sections were filled with i inch (0.64 cm) Intalox saddles. In the first experiment for which mesityl oxide was synthesized from acetone, the two sections were filled with 130 mL of Amberlyst-15, that had been swelled in 2-propanol for 24 hours, in wire mesh bundles. In the second experiment in which MIBK was synthesized from acetone, the top section and the top half of the bottom section contained 135.0 mL of Amberlyst-15 in wire mesh bundles that had been swelled in acetone for over 24 hours. The bottom half of the bottom section, immediately below the Amberlyst 15, was filled with 50.1 g of a commercial Pd/AlzOs catalyst (Aldrich 20,574-5). The hydrogenation catalyst was reduced ex situ in hydrogen at 350°C for 3 hours and was transferred to the CD column under a nitrogen blanket. [Pg.368]

Figure 1337. Corn-elation of flow rates, typical pressure drop behavior, and packing factors of random packed beds. [Eckert, Foote, and Walter, Chem. Eng. Prog. 62(1), 59 (1966) Eckert, Chem. Eng. 14 Apr. 1975)]. (a) Correlation of flow rate and pressure drop in packed towers, (b) Typical pressure drop data 2 in. porcelain intalox saddles, with F = 40, in a bed 30 in. dia by 10 ft high, (c) Packing factors, F, of wet random packings-... Figure 1337. Corn-elation of flow rates, typical pressure drop behavior, and packing factors of random packed beds. [Eckert, Foote, and Walter, Chem. Eng. Prog. 62(1), 59 (1966) Eckert, Chem. Eng. 14 Apr. 1975)]. (a) Correlation of flow rate and pressure drop in packed towers, (b) Typical pressure drop data 2 in. porcelain intalox saddles, with F = 40, in a bed 30 in. dia by 10 ft high, (c) Packing factors, F, of wet random packings-...
The amount of liquid holdup in the packing is of interest when the liquid is unstable or when a desirable reaction is to be carried out in the vessel. A correlation for Raschig rings, Berl saddles, and intalox saddles is due to Leva (Tower Packings and Packed Tower Design, U.S. Stoneware Co., Akron, OH, (1953) ... [Pg.439]

Intalox saddles and pall rings of 1-1.5-in. size are the most commonly used packings. Smaller sizes tend to be less effective since their voids are of the same order of magnitude as drop... [Pg.482]

Berl Saddles. P ieces of chemical porcelain, chemical stoneware or carbon in the shape of saddles, used for packing absorption tower or distn columns. They are manufd under trade name "Intalox Saddles" by the US Stoneware Co, Akron 9, Ohio... [Pg.104]

Table II shows that, as packing size increases, packing capacity rises while packing efficiency decreases. It also shows that both capacity and efficiency are greater for Pall rings and Intalox saddles than for Raschig rings and Berl saddles. Table II shows that, as packing size increases, packing capacity rises while packing efficiency decreases. It also shows that both capacity and efficiency are greater for Pall rings and Intalox saddles than for Raschig rings and Berl saddles.
Figure 8.2 Second-generation random packings, (a) Intalox saddle, ceramic (6) Super Intalox saddle, ceramic (Courtesy of Norton Company.)... Figure 8.2 Second-generation random packings, (a) Intalox saddle, ceramic (6) Super Intalox saddle, ceramic (Courtesy of Norton Company.)...
Intalox saddles are available in ceramic only from the Norton Company. Packings that are normally considered equivalent to the Intalox saddles are marketed under the trade names of Flexisaddle by Koch Engineering Company, Inc. and Novalox saddles by Jaeger... [Pg.425]

Figure 7 illustrates in schematic fashion the three column DBBP solvent extraction system. All three columns are made of 304L stainless steel columns and are packed with 1-inch Kynar (Pennwalt Corp.) Intalox saddles. Aqueous and organic phases are mixed by means of air pulses supplied to each column. Important column dimensions are shown in Figure 7. [Pg.125]

Saddle-shaped packings, such as Intalox saddles and Berl saddles, are available in sizes from j to 2 in. These packings are formed from chemical stoneware, plastics, or any other material that can be shaped by punch dies. They form an interlocking structure which gives less side thrust and more active surface area per unit volume than Raschig rings. [Pg.689]


See other pages where Packings Intalox saddles is mentioned: [Pg.1757]    [Pg.71]    [Pg.235]    [Pg.1751]    [Pg.1757]    [Pg.71]    [Pg.235]    [Pg.1751]    [Pg.171]    [Pg.1366]    [Pg.1476]    [Pg.247]    [Pg.271]    [Pg.87]    [Pg.316]    [Pg.301]    [Pg.591]    [Pg.599]    [Pg.694]    [Pg.435]    [Pg.24]    [Pg.54]    [Pg.54]    [Pg.118]    [Pg.282]    [Pg.269]    [Pg.424]    [Pg.247]    [Pg.271]    [Pg.68]    [Pg.688]    [Pg.199]   
See also in sourсe #XX -- [ Pg.154 ]




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