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Mass load paths

Trading off Rxed versus operating costs using mass-load paths... [Pg.119]

Tradiiig Off Fixed versus Operating Costs Using Mass-Load Paths... [Pg.119]

Three additional mass-load paths S3-R2-S2, S3-R1-S1, S3-R1-S2 ) can be employed to shift removal duties from the process MSAs to the external MSA until all the waste load (0.104 kg phenol/s) is removed by the external MSA... [Pg.121]

Using the cascade diagram, solve Problem 3.3. Also, synthesize an MEN which h the minimum number of units satisfying the MOC solution. Employ the mass-load paths to reduce the number of mass exchangers at the expense of increasing operating cost. [Pg.123]

By comparing Eqs. (3.29) and (5.16), we notice that the s licmicHi of the mass-load paths has resulted in an increase of die op dng cost of 2,129 million/yr. On the odier hand, die numher of mass exchange has drqpped from seven to two. The extent to which the fixed cost of the mai exchangeis has decreased determines whether or not this increase in operating cost is acceptable. [Pg.123]

Where several units of the same type are mounted within a space, discrete frequencies will be amplified and beat notes will be apparent. Special treatment is usually called for, in the way of indirect air paths and mass-loaded panels [10, 19, 56, 60]. [Pg.315]

Fig. 21. A surface acoustic wave dual-delay line oscillator. The sensitise layer is placed in the propagation path of one of the two SAW devices. The differenee in Ireqnency (At) between the two channels provides a dtrecl result of the mass loading and electric field effects associated w ith the sensor layer... Fig. 21. A surface acoustic wave dual-delay line oscillator. The sensitise layer is placed in the propagation path of one of the two SAW devices. The differenee in Ireqnency (At) between the two channels provides a dtrecl result of the mass loading and electric field effects associated w ith the sensor layer...
The analysis results in Figure 1 are from a numerical transient thermal and structural collapse analysis, where heat conduction is included and where the structural stiffness (and hence the load path) is computed for every time step in the solution process. This analysis is more accurate than the former because it includes the composite action of the three dimensional imevenly heated structure, where the load path is shed from the hot to the cold members. The method therefore represents the structural redimdancy and gives (more accurately) longer times to collapse than the lumped thermal mass method. [Pg.2079]

To minimize the multiple path and mass transfer contributions to plate height (equations 12.23 and 12.26), the packing material should be of as small a diameter as is practical and loaded with a thin film of stationary phase (equation 12.25). Compared with capillary columns, which are discussed in the next section, packed columns can handle larger amounts of sample. Samples of 0.1-10 )J,L are routinely analyzed with a packed column. Column efficiencies are typically several hundred to 2000 plates/m, providing columns with 3000-10,000 theoretical plates. Assuming Wiax/Wiin is approximately 50, a packed column with 10,000 theoretical plates has a peak capacity (equation 12.18) of... [Pg.564]

The transient response of DMFC is inherently slower and consequently the performance is worse than that of the hydrogen fuel cell, since the electrochemical oxidation kinetics of methanol are inherently slower due to intermediates formed during methanol oxidation [3]. Since the methanol solution should penetrate a diffusion layer toward the anode catalyst layer for oxidation, it is inevitable for the DMFC to experience the hi mass transport resistance. The carbon dioxide produced as the result of the oxidation reaction of methanol could also partly block the narrow flow path to be more difScult for the methanol to diflhise toward the catalyst. All these resistances and limitations can alter the cell characteristics and the power output when the cell is operated under variable load conditions. Especially when the DMFC stack is considered, the fluid dynamics inside the fuel cell stack is more complicated and so the transient stack performance could be more dependent of the variable load conditions. [Pg.593]

Micro-injections in micro-flow and nano-flow systems are done with injectors in which the external sample loop is replaced with the internal fixed volume within the injector body. HPLC-on-a-chip systems also build the column into the injector body. The internal path within the injector body is abladed with a laser, packed with micro-packing material, and this serves as the separating media. The injector inlet is connected to the pumping system and the outlet to the detector. Sample is loaded into an internal loop in the load position, then injected onto the chip HPLC by turning the injector. Obviously, in a system like this sample size is very limited and the detector is usually a highly sensitive mass spectrometer. [Pg.116]


See other pages where Mass load paths is mentioned: [Pg.119]    [Pg.121]    [Pg.123]    [Pg.146]    [Pg.119]    [Pg.121]    [Pg.121]    [Pg.146]    [Pg.119]    [Pg.121]    [Pg.123]    [Pg.146]    [Pg.119]    [Pg.121]    [Pg.121]    [Pg.146]    [Pg.1025]    [Pg.337]    [Pg.128]    [Pg.130]    [Pg.386]    [Pg.75]    [Pg.157]    [Pg.2587]    [Pg.480]    [Pg.162]    [Pg.156]    [Pg.498]    [Pg.499]    [Pg.405]    [Pg.743]    [Pg.33]    [Pg.178]    [Pg.575]    [Pg.191]    [Pg.11]    [Pg.167]    [Pg.280]   
See also in sourсe #XX -- [ Pg.119 ]

See also in sourсe #XX -- [ Pg.119 ]




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