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Mixing, heat partial

Manual calculations are also very useful when solving flowsheets that use recycle and purge. Purge streams are often withdrawn from recycles to prevent the accumulation of species that are difficult to separate, as described in Section 2.15. A typical recycle and purge flow scheme is illustrated in Figure 4.42. A liquid feed and a gas are mixed, heated, reacted, cooled and separated to give a liquid product. Unreacted gas from the separator is recycled to the feed. A make-up stream is added to the gas recycle to make up for consumption of gas in the process. If the make-up gas contains any inert gases, then over time these would accumulate in the recycle and eventually the reaction would be slowed down when the partial pressure of reactant... [Pg.212]

Thus hf is equal to the heat absorbed (per mole of 1) when a small quantity 8ui of substance 1 is dissolved in the solution at constant T and p. For this reason it is often called the heat of solution of component 1, differential heat of mixing or partial molar heat of mixing." The partial molar heats may be determined readily from the heat of mixing h by the Bakhuis-Rooseboom method described in 3 of chap. I. [Pg.384]

K. R. Sharma, Dimensionless Ratio of Heat Capacity Change to that of Entropy of Mixing for Partially Miscible Polymer Blends, 95th AIChE Annnal Meeting, San Francisco, November 2003. [Pg.141]

Savim, C. G. Winterhalter, D. R- Van Ness, H. C. Heats of mixing for partially miscible systems methanol - n hp-r j methanol - n-heptane J. Chem. Eng. Data 1965,10,171-172... [Pg.1263]

Ambali is produced from a naturally occurring lactic acid bacteria that ferments a paste produced from finger millet. After fermentation, the paste is mixed with partially cooked rice and heated until completely cooked. Then the mixture is allowed to cool down and flavored with sour milk before consumption (Steinkraus 1983, 1989). [Pg.548]

Typical altitude profiles of pollutants downwind of India, measured from the C-130 aircraft, also show the residual layer (Fig. 9.5b). In general, this layer was more pronounced in March than in February, related to the growing convection over land as surface heating increases toward the end of winter. Some of the profiles also show a secondary maximum between 3- and 4-km altitude. Meteorological analysis indicates that these air masses were transported from the east, carrying pollution from Southeast Asia. On several occasions, it was observed that the vertical layering, shown in Fig. 9.5, can be maintained as far south as the Maldives, whereas further toward the ITCZ, trade wind cumulus convection causes breakup, vertical mixing, and partial dispersion into the free troposphere. [Pg.205]

The reactor effluent might require cooling by direct heat transfer because the reaction needs to be stopped quickly, or a conventional exchanger would foul, or the reactor products are too hot or corrosive to pass to a conventional heat exchanger. The reactor product is mixed with a liquid that can be recycled, cooled product, or an inert material such as water. The liquid vaporizes partially or totally and cools the reactor effluent. Here, the reactor Teed is a cold stream, and the vapor and any liquid from the quench are hot streams. [Pg.329]

Noncatalytic partial oxidation of residual fuel oil accounts for the remainder of world methanol production. Shell and Texaco ate the predominant hcensors for partial oxidation technology (16) the two differ principally in the mechanical details of mixing the feedstock and oxidant, in waste heat recovery, and in soHds management. [Pg.278]

Plants producing oleum or Hquid SO typically have one or two additional packed towers irrigated with oleum ahead of the normal SO absorption towers. Partial absorption of SO occurs in these towers, and sulfuric acid is added to maintain desired oleum concentrations. Normally, oleum up to about 35 wt % free SO content can be made in a single tower two towers are used for 40 wt % SO. Liquid SO is produced by heating oleum in a boder to generate SO gas, which is then condensed. Oleums containing SO >40 wt % are usually produced by mixing SO with low concentration oleum. [Pg.183]

As in the case of biphenyl, current worldwide production figures for terphenyls are not readily obtainable, but the volume is probably around 6.8—8.2 million kg/yr. Currently, most of the terphenyl produced is converted to a partially hydrogenated form. U.S. production of terphenyls has remained steady at several thousand metric tons per year over the past decade. The 1991 small lot price for mixed terphenyls was about 3.89/kg whereas the specially fractionated heat-transfer-grade terphenyl—quaterphenyl mixture sold as Therminol 75 heat-transfer fluid was priced around 6.93/kg. Partially hydrogenated mixed terphenyls were priced in the 6.05—7.48/kg range depending on quantity and grade. [Pg.117]


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Mixing heat

Partial molar heat of mixing

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