Gas absorption and oxidation in dispersed media

Andersen, L. B.; Johnstone, H. F.

doi:10.1002/aic.690010202

Cited by 9 publications

(1 citation statement)

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“…Since Comings' study (1948) on the heat transfer in a venturi scrubber many studies on the venturi-tvpe scrubbers have appeared in the literature (Anderson and Johnstone, 1955;Boyadzhiev, 1964;Elenkov and Boyadzhiev, 1967;Feild, 1950;Gleason, 1971;Harris, 1971;Johnstone, et al, 1954;Johnstone and Robert, 1949; Kuznetsov and Oratovskii, 1962;Markant, et al 1962;Tassler, 1952;Volgin, et al 1968). Johnstone and Robert (1949), Feild (1950), and Johnstone, et al (1954), investigated the absorption of sulfur dioxide in water and alkaline solutions and measured the amount of sulfur dioxide absorbed in the liquid at various distances from the point of liquid injection in a venturi scrubber.…”

Section: Previous Studiesmentioning

confidence: 99%

Gas Absorption by Alkaline Solutions in a Venturi Scrubber

Uchida¹,

Wen²

1973

Ind. Eng. Chem. Proc. Des. Dev.

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Section: Previous Studiesmentioning

confidence: 99%

Gas Absorption by Alkaline Solutions in a Venturi Scrubber

Uchida¹,

Wen²

1973

Ind. Eng. Chem. Proc. Des. Dev.

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A kinetic study of sulfur dioxide in aqueous solution with radioactive tracers

Wang

Himmelblau

1964

AIChE Journal

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Selective absorption of H₂S from larger quantities of CO₂ by absorption and reaction in fine sprays

1983

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Highly selective transfer of hydrogen sulfide (HzS) from much larger quantities of carbon dioxide (COZ) has been accomplished by absorption and reaction into fine sprays of buffered carbonate solution. Selectivity after the intensely agitated atomization zone is dramatically improved once the droplets have formed and stagnate internally. HZS transfer in this latter zone is virtually independent of the presence of COz, even at C02:HzS ratios of 1cO; COZ transfer, however, is adversely affected by the presence of H2S. The gas film resistance for mass transfer is effectively eliminated with the 50 p m mean droplet diameter. The data indicate approximately constant hydrodynamics throughout the formed droplet zone and allow.good theoretical prediction of enhancement factors for this complex system. Thus the design of more efficient equipment is possible if the gas-liquid contacting method is tailored to take advantage of differences in the transfer and reaction rate properties of gases to be separated. E. BENDALL, R. C. AIKEN, and F. MANDAS Department of Chemical EngineeringUniversity of Utah Salt Lake City, UT 84112The need for a selective separation of HzS from COz occurs as it is often too expensive and not necessary to remove large quantities of COz along with the pollutant HzS. Often no process is capable of removing the H2S to specifications without uneconomical removal of the majority of the COz, thus requiring a large purification plant and large capital investment. Situations in which HZS and larger quantities of COz appear include low to medium BTU gas wells or natural COz sources, and in fossil fuel plants operating under partial oxidative environments.There have been few experimental or theoretical studies of mass transfer into a dispersed medium with subsequent intraphase reaction. Applications include topics in liquid-liquid extraction and gas purification where single components are transferred or multiple competitively or synergistically interacting components are transferred. Description of the fluid dynamics for such systems is complicated by the existence of three different regimes always present: atomization, droplet flight, and coalescence. Many atomization techniques exist and none are welldescribed for sprays. Atomization greatly affects the droplet flight regime as it determines the droplet size distribution, dynamics and interaction. Continuous phase backmixing and internal dispersed-phase mixing further can complicate the theoretical description of the fluid dynamics.This article contains a summary of an experimental study on selective removal of HzS from much larger quantities of COz using a conventional liquid solution but sprayed into a chamber as a fine mist. The primary variable between runs was the amount of liquid reagent in solution. Gas and liquid samples were taken throughout the reactor. CONCLUSIONS AND SIGNIFICANCEThere is a significant increase in selective and extensive transport of H2S over COz if the scrubbing liquid is finely divided. This advantage is particularly great outs...

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Gas absorption and oxidation in dispersed media

Cited by 9 publications

References 5 publications

Gas Absorption by Alkaline Solutions in a Venturi Scrubber

Gas Absorption by Alkaline Solutions in a Venturi Scrubber

A kinetic study of sulfur dioxide in aqueous solution with radioactive tracers

Selective absorption of H₂S from larger quantities of CO₂ by absorption and reaction in fine sprays

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Gas absorption and oxidation in dispersed media

Cited by 9 publications

References 5 publications

Gas Absorption by Alkaline Solutions in a Venturi Scrubber

Gas Absorption by Alkaline Solutions in a Venturi Scrubber

A kinetic study of sulfur dioxide in aqueous solution with radioactive tracers

Selective absorption of H2S from larger quantities of CO2 by absorption and reaction in fine sprays

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Selective absorption of H₂S from larger quantities of CO₂ by absorption and reaction in fine sprays