Abstract
A method for production and purification of pyrocatechol (I) from low-temperature carbonization effluents was described. Phenosolvan, a mixture of isobutyl, butyl, and amyl acetates, was used for extraction of I from the effluent. After removing most of the solvent by distillation, the separation was completed by batch vacuum distillation at 25 to 50 millimeter Hg. The 4th fraction, containing I 49.2, I homologues 31.1, o-cresol 6.8, xylenols 7.3, and higher boiling material and residue 5.6 percent, was treated in a purification pilot plant, which was described. This fraction was dissolved in an equal weight of C/sub 6/H/sub 6/, then cooled. I was crystallized out in a vacuum crystallizer, centrifuged, and washed with C/sub 6/H/sub 6/, dried in a rotating-plate drier and taken to storage. The purified I melted 100/sup 0/ to 102/sup 0/ and contained 4 to 8 percent homologues or other impurities. A further recrystallization raised its purity to 99.2 percent. Plant capacities and production costs are given.
Citation Formats
Lowenstein-Lom, W.
Pyrocatechol from low-temperature tar.
United Kingdom: N. p.,
1950.
Web.
Lowenstein-Lom, W.
Pyrocatechol from low-temperature tar.
United Kingdom.
Lowenstein-Lom, W.
1950.
"Pyrocatechol from low-temperature tar."
United Kingdom.
@misc{etde_5392171,
title = {Pyrocatechol from low-temperature tar}
author = {Lowenstein-Lom, W}
abstractNote = {A method for production and purification of pyrocatechol (I) from low-temperature carbonization effluents was described. Phenosolvan, a mixture of isobutyl, butyl, and amyl acetates, was used for extraction of I from the effluent. After removing most of the solvent by distillation, the separation was completed by batch vacuum distillation at 25 to 50 millimeter Hg. The 4th fraction, containing I 49.2, I homologues 31.1, o-cresol 6.8, xylenols 7.3, and higher boiling material and residue 5.6 percent, was treated in a purification pilot plant, which was described. This fraction was dissolved in an equal weight of C/sub 6/H/sub 6/, then cooled. I was crystallized out in a vacuum crystallizer, centrifuged, and washed with C/sub 6/H/sub 6/, dried in a rotating-plate drier and taken to storage. The purified I melted 100/sup 0/ to 102/sup 0/ and contained 4 to 8 percent homologues or other impurities. A further recrystallization raised its purity to 99.2 percent. Plant capacities and production costs are given.}
journal = []
volume = {13}
journal type = {AC}
place = {United Kingdom}
year = {1950}
month = {Jan}
}
title = {Pyrocatechol from low-temperature tar}
author = {Lowenstein-Lom, W}
abstractNote = {A method for production and purification of pyrocatechol (I) from low-temperature carbonization effluents was described. Phenosolvan, a mixture of isobutyl, butyl, and amyl acetates, was used for extraction of I from the effluent. After removing most of the solvent by distillation, the separation was completed by batch vacuum distillation at 25 to 50 millimeter Hg. The 4th fraction, containing I 49.2, I homologues 31.1, o-cresol 6.8, xylenols 7.3, and higher boiling material and residue 5.6 percent, was treated in a purification pilot plant, which was described. This fraction was dissolved in an equal weight of C/sub 6/H/sub 6/, then cooled. I was crystallized out in a vacuum crystallizer, centrifuged, and washed with C/sub 6/H/sub 6/, dried in a rotating-plate drier and taken to storage. The purified I melted 100/sup 0/ to 102/sup 0/ and contained 4 to 8 percent homologues or other impurities. A further recrystallization raised its purity to 99.2 percent. Plant capacities and production costs are given.}
journal = []
volume = {13}
journal type = {AC}
place = {United Kingdom}
year = {1950}
month = {Jan}
}