Vapor-liquid equilibria for α-pinene and β-pinene with 1-butanol and 1-pentanol

Reich, Ronny; Sanhueza, Vilma

doi:10.1016/0378-3812(92)87038-o

Cited by 15 publications

(10 citation statements)

References 12 publications

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“…Isobaric VLB information for -pinene + 3-pinene and for these pinenes with other terpene hydrocarbons like limonene, terpinolene, A3-carene, p-cymene, and 1,8-cineole is available in the literature (3)(4)(5)(6)(7). Only recently, isothermal P-x-y VLB data for -pinene and 3-pinene with heptane, cyclohexane, 1-octene, cyclohexene, 1-butanol, and 1-pentanol, and infinite dilute activity coefficients for these same systems and with aromatics and ethers have been measured and published (8)(9)(10).…”

Section: Introductionmentioning

confidence: 99%

Vapor-liquid equilibria for .alpha.-pinene or .beta.-pinene with anisole

Reich¹,

Sanhueza²

1993

J. Chem. Eng. Data

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Section: Introductionmentioning

confidence: 99%

Vapor-liquid equilibria for .alpha.-pinene or .beta.-pinene with anisole

Reich¹,

Sanhueza²

1993

J. Chem. Eng. Data

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“…For this study, the parameters are required for a pressure range of 30-100 mbar. As the available literature data [32][33][34][35][36][37][38][39][40][41][42][43][44] show considerable differences of up to 38C for the boiling point temperatures at low pressures, measurements of the boiling points have been carried out for all components. A literature review for the vaporliquid-equilibria showed that only for the system 1-butanol/ n-butyl acetate accurate literature data are available.…”

Section: Vapor-liquid-equilibrium Datamentioning

confidence: 99%

Enzymatic catalyzed reactive dividing wall column: Experiments and model validation

Egger

Fieg

2016

AIChE Journal

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A novel process for the integration of chemical reaction and product separation is proposed: the enzymatic catalyzed reactive dividing wall column (eRDWC). The eRDWC combines the highly integrated and complex reactive dividing wall column (RDWC) with the use of a very selective enzymatic catalyst. This apparatus enables the simultaneous production and separation of up to 4 pure product streams. Comprehensive experiments with the reference system of a hexanol and butyl acetate transesterification in a DN 65 pilot scale column show the feasibility of stable steady state operations for this process. A rigorous model for the plant design of an eRDWC wall column is developed. The reaction kinetics and vapor‐liquid‐equilibria for the reference system are measured and implemented in the model. The model is successfully validated using the acquired experimental data. The application of enzymes in continuous reactive distillation processes has the potential to increase the selectivity at milder process conditions. © 2016 American Institute of Chemical Engineers AIChE J, 63: 2198–2211, 2017

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“…The binary isobaric (vapour + liquid) equilibria (VLE) data for a-pinene with terpene hydrocarbons, and isothermal VLE data for a-pinene with alkanes, alkenes, and n-alkanols are available in the literature [2][3][4][5]. The ternary VLE data of (a-pinene + n-butanol + n-octane) are scarce in the literature.…”

Section: Introductionmentioning

confidence: 98%