Our system is currently under heavy load due to increased usage. We're actively working on upgrades to improve performance. Thank you for your patience.
1966
DOI: 10.1021/i260017a001
|View full text |Cite
|
Sign up to set email alerts
|

Fixed-Bed Drying of Air Using Molecular Sieves

Abstract: The rate of drying of air in a fixed bed of molecular sieves was investigated. Exit air moisture content as a function of time was measured at several values of inlet concentration, flow rate, fixed-bed height, and bed temperature. Over-all, solid phase, and gas phase mass transfer coefficients and particle and pore diffusivities were calculated. The pore diffusion model of Vermeulen and Acrivos best reproduced experimental data and is recommended as a basis for design calculations.^he adsorption process for f… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1

Citation Types

0
3
0

Year Published

1967
1967
2021
2021

Publication Types

Select...
6
1

Relationship

0
7

Authors

Journals

citations
Cited by 15 publications
(3 citation statements)
references
References 0 publications
0
3
0
Order By: Relevance
“…The lack of dependence on pressure indicates that the diffusion mechanism in the adsorbent is either surface migration or Knudscn diffusion, or a combination of these, rather than bulk (or molecular) diffusion. Second, although the data show considerable scatter, it is obvious that k s is a function of Co' The large experimental scatter .in k s values is also apparent in the data of Eagleton and Bliss [7] as weH as that of Nutter and Burnet [13], and is principaHy due to the fact that the value of k s depends on the ratio of the slope of the In(l -C/C o ) VS. t curve to that of the In CIC o VS. t curve. Since, in many instances, these curves are not too linear, it is often very difficult to determine the best value of the slopes.…”
Section: Evaluation Of Mass Transfer Coefficientsmentioning
confidence: 89%
“…The lack of dependence on pressure indicates that the diffusion mechanism in the adsorbent is either surface migration or Knudscn diffusion, or a combination of these, rather than bulk (or molecular) diffusion. Second, although the data show considerable scatter, it is obvious that k s is a function of Co' The large experimental scatter .in k s values is also apparent in the data of Eagleton and Bliss [7] as weH as that of Nutter and Burnet [13], and is principaHy due to the fact that the value of k s depends on the ratio of the slope of the In(l -C/C o ) VS. t curve to that of the In CIC o VS. t curve. Since, in many instances, these curves are not too linear, it is often very difficult to determine the best value of the slopes.…”
Section: Evaluation Of Mass Transfer Coefficientsmentioning
confidence: 89%
“…The concept of a zeolite resistance also leads to a significant improvement in the interpretation of the data of Nutter and Burnet (1966) for air drying in a fixed bed of molecular sieves. Nutter and Burnet's calculated values of Dpore varied by a factor of 7 over a fourfold range of particle sizes, whereas Z)pore should be independent of the particle size.…”
Section: Analysis Of Adsorption Rate Experimentsmentioning
confidence: 99%
“…A survey of the literature shows intensive studies of silica gel (Bullock, 1965;Bullock and Threlkeld, 1966;Elstonalberg, 1939;Hubard, 1954;Simpson and Cummings, 1964). Molecular sieves (Barrer, 1964;Greismer et al, 1959;Hougen and Dodge, 1947;Nutter and Barnet, 1966), activated alumina (Eagleton and Bliss 1953;Fleming et al, 1964;Getty and Armstrong, 1964), and activated carbon (Allman et al, 1929) have received considerable attention. Work has also been reported on hygroscopic salts such as calcium chloride (Baxter and Starkweather, 1916;Baxter and Warren, 1911), barium oxide (Booth and McIntyre, 1930), and perchlorates (Hammond and Withrow, 1933;Lenher and Taylor, 1930).…”
mentioning
confidence: 99%