Influence of alkylaromatic hydrocarbons on the efficiency of linear alkylbenzene sulfonic acid synthesis; Chemical Engineering Journal; Vol. 329 : XXII International conference on Chemical Reactors CHEMREACTOR-22, 1 December 2017

Bibliografiske detaljer
Parent link:Chemical Engineering Journal
Vol. 329 : XXII International conference on Chemical Reactors CHEMREACTOR-22, 1 December 2017.— 2017.— [P. 250-261]
Institution som forfatter: Национальный исследовательский Томский политехнический университет (ТПУ) Институт природных ресурсов (ИПР) Кафедра химической технологии топлива и химической кибернетики (ХТТ)
Andre forfattere: Ivanchina E. D. Emilia Dmitrievna, Ivashkina E. N. Elena Nikolaevna, Dolganova I. O. Irena Olegovna, Frantsina E. V. Evgeniya Vladimirovna, Dolganov I. M. Igor Mikhailovich
Summary:Title screen
ASA is the main ingredient of many commercial formulations for industrial and domestic synthetic detergents. Studying the work of the technological equipment that is used for manufacturing of the linear ASA allow us to conclude that alkylaromatic hydrocarbons in the product flow to hydrogenation reactor have significant impact on all technological stages. The aim of this work was to estimate the quantitative impact of alkyl components on ASA manufacturing efficiency and to improve the performance of the main equipment. The performed infrared (IR) and gas chromatography–mass spectrometry (GC–MS) analysis of the linear alkylbenzenes (LAB) and ASA samples indicate that the viscous components are tetralines and sultones as a part of unsulphonated matter. The developed mathematical model was used to reveal the following results and regularities of equipment modes: if the hydrogen/feedstock molar ratio at dehydrogenation stage equals 6/1, it is less optimal due to coke formation and requires increasing water supply. An increase of aromatics content in alkylation product flow leads to an increase in HF flow rate to the regeneration column. The optimal SO3/LAB molar ratio increases along with content of aromatics in raw materials. The developed model of sulfonation process predicts the duration of reactor inter-washing period.
Режим доступа: по договору с организацией-держателем ресурса
Sprog:engelsk
Udgivet: 2017
Fag:
Online adgang:https://doi.org/10.1016/j.cej.2017.06.032
Format: Electronisk Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=656439

MARC

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200 1 |a Influence of alkylaromatic hydrocarbons on the efficiency of linear alkylbenzene sulfonic acid synthesis  |f E. D. Ivanchina [et al.] 
203 |a Text  |c electronic 
300 |a Title screen 
320 |a [References: 45 tit.] 
330 |a ASA is the main ingredient of many commercial formulations for industrial and domestic synthetic detergents. Studying the work of the technological equipment that is used for manufacturing of the linear ASA allow us to conclude that alkylaromatic hydrocarbons in the product flow to hydrogenation reactor have significant impact on all technological stages. The aim of this work was to estimate the quantitative impact of alkyl components on ASA manufacturing efficiency and to improve the performance of the main equipment. The performed infrared (IR) and gas chromatography–mass spectrometry (GC–MS) analysis of the linear alkylbenzenes (LAB) and ASA samples indicate that the viscous components are tetralines and sultones as a part of unsulphonated matter. The developed mathematical model was used to reveal the following results and regularities of equipment modes: if the hydrogen/feedstock molar ratio at dehydrogenation stage equals 6/1, it is less optimal due to coke formation and requires increasing water supply. An increase of aromatics content in alkylation product flow leads to an increase in HF flow rate to the regeneration column. The optimal SO3/LAB molar ratio increases along with content of aromatics in raw materials. The developed model of sulfonation process predicts the duration of reactor inter-washing period. 
333 |a Режим доступа: по договору с организацией-держателем ресурса 
461 |t Chemical Engineering Journal 
463 |t Vol. 329 : XXII International conference on Chemical Reactors CHEMREACTOR-22, 1 December 2017  |v [P. 250-261]  |d 2017 
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701 1 |a Ivanchina  |b E. D.  |c chemist  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1951-  |g Emilia Dmitrievna  |3 (RuTPU)RU\TPU\pers\31274 
701 1 |a Ivashkina  |b E. N.  |c Chemical Engineer  |c Professor of Tomsk Polytechnic University, Doctor of technical sciences  |f 1983-  |g Elena Nikolaevna  |3 (RuTPU)RU\TPU\pers\31275  |9 15453 
701 1 |a Dolganova  |b I. O.  |c chemist  |c Associate Scientist of Tomsk Polytechnic University, postgraduate student, candidate of technical Sciences  |f 1988-  |g Irena Olegovna  |3 (RuTPU)RU\TPU\pers\31271  |9 15449 
701 1 |a Frantsina  |b E. V.  |c Chemical Engineer  |c Associate Professor of Tomsk Polytechnic University, Candidate of technical sciences  |f 1985-  |g Evgeniya Vladimirovna  |3 (RuTPU)RU\TPU\pers\32193  |9 16193 
701 1 |a Dolganov  |b I. M.  |c Chemical Engineer  |c Associate Professor of Tomsk Polytechnic University, Candidate of Technical Sciences  |f 1987-  |g Igor Mikhailovich  |3 (RuTPU)RU\TPU\pers\32216  |9 16216 
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