Calculation of a packed column for absorption of hydrogen sulfur from gases formed by separation of crude oil

According to the well-known calculating algorithm for the packed absorption column, the main technological parameters and geometric dimensions of the apparatus for hydrogen sulfide containing gases, formed during the separation of crude oil, are determined. A 2,5-n solution of monoethanolamine is se...

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Main Authors: Golovanchikov A.B., Churikova V.I., Zalipaeva O.A.
Format: Article
Language:English
Published: EDP Sciences 2019-01-01
Series:E3S Web of Conferences
Online Access:https://www.e3s-conferences.org/articles/e3sconf/pdf/2019/52/e3sconf_icmtmte2019_00070.pdf
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spelling doaj-7a87b6820828411d9b313d6aa32e1b842021-02-02T08:41:25ZengEDP SciencesE3S Web of Conferences2267-12422019-01-011260007010.1051/e3sconf/201912600070e3sconf_icmtmte2019_00070Calculation of a packed column for absorption of hydrogen sulfur from gases formed by separation of crude oilGolovanchikov A.B.Churikova V.I.Zalipaeva O.A.According to the well-known calculating algorithm for the packed absorption column, the main technological parameters and geometric dimensions of the apparatus for hydrogen sulfide containing gases, formed during the separation of crude oil, are determined. A 2,5-n solution of monoethanolamine is selected as the absorbent. Comparative results of the calculations are showing, that the working pressure in the column should be 4 atm, since with their lower values, the flow rate of the absorbent and the size of the column are increasing. The increase in working pressure is impractical, since it will require a transition from centrifugal and compresses pumps to piston pumps. ∏ The obtained parameters were compared for an absorption column in which the flow structure of the gas and liquid phases corresponds to ideal displacement, with the calculation results when the flow structure in the gas phase corresponds to the ideal displacement mode (as in the standard calculation algorithm) and in the liquid phase to ideal mixing. It is shown that, with the Peclet number of longitudinal diffusion pe<40 the height and volume of the column increases by 10 and more percent and should be taken into account when packed columns, intended for absorption processes, are designed. At pe=30 the height and volume of the nozzle in the column increases by 27%. Another feature of the modelling and calculation of devices is a spike in concentration, meaning, that the lower part of the working line will cross the equilibrium. Calculations in thisparticular case show that at ≈ 11 the working line crosses the equilibrium and theoretically column height and volume →∞.https://www.e3s-conferences.org/articles/e3sconf/pdf/2019/52/e3sconf_icmtmte2019_00070.pdf
collection DOAJ
language English
format Article
sources DOAJ
author Golovanchikov A.B.
Churikova V.I.
Zalipaeva O.A.
spellingShingle Golovanchikov A.B.
Churikova V.I.
Zalipaeva O.A.
Calculation of a packed column for absorption of hydrogen sulfur from gases formed by separation of crude oil
E3S Web of Conferences
author_facet Golovanchikov A.B.
Churikova V.I.
Zalipaeva O.A.
author_sort Golovanchikov A.B.
title Calculation of a packed column for absorption of hydrogen sulfur from gases formed by separation of crude oil
title_short Calculation of a packed column for absorption of hydrogen sulfur from gases formed by separation of crude oil
title_full Calculation of a packed column for absorption of hydrogen sulfur from gases formed by separation of crude oil
title_fullStr Calculation of a packed column for absorption of hydrogen sulfur from gases formed by separation of crude oil
title_full_unstemmed Calculation of a packed column for absorption of hydrogen sulfur from gases formed by separation of crude oil
title_sort calculation of a packed column for absorption of hydrogen sulfur from gases formed by separation of crude oil
publisher EDP Sciences
series E3S Web of Conferences
issn 2267-1242
publishDate 2019-01-01
description According to the well-known calculating algorithm for the packed absorption column, the main technological parameters and geometric dimensions of the apparatus for hydrogen sulfide containing gases, formed during the separation of crude oil, are determined. A 2,5-n solution of monoethanolamine is selected as the absorbent. Comparative results of the calculations are showing, that the working pressure in the column should be 4 atm, since with their lower values, the flow rate of the absorbent and the size of the column are increasing. The increase in working pressure is impractical, since it will require a transition from centrifugal and compresses pumps to piston pumps. ∏ The obtained parameters were compared for an absorption column in which the flow structure of the gas and liquid phases corresponds to ideal displacement, with the calculation results when the flow structure in the gas phase corresponds to the ideal displacement mode (as in the standard calculation algorithm) and in the liquid phase to ideal mixing. It is shown that, with the Peclet number of longitudinal diffusion pe<40 the height and volume of the column increases by 10 and more percent and should be taken into account when packed columns, intended for absorption processes, are designed. At pe=30 the height and volume of the nozzle in the column increases by 27%. Another feature of the modelling and calculation of devices is a spike in concentration, meaning, that the lower part of the working line will cross the equilibrium. Calculations in thisparticular case show that at ≈ 11 the working line crosses the equilibrium and theoretically column height and volume →∞.
url https://www.e3s-conferences.org/articles/e3sconf/pdf/2019/52/e3sconf_icmtmte2019_00070.pdf
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