Distillation: processes – separatory – Adding material to distilland except water or steam per se – Organic compound
Reexamination Certificate
1995-04-11
2001-10-09
Manoharan, Virginia (Department: 1764)
Distillation: processes, separatory
Adding material to distilland except water or steam per se
Organic compound
C203S018000, C203S037000, C203S057000, C203S071000, C568S868000
Reexamination Certificate
active
06299737
ABSTRACT:
The present invention relates to an improved process for recovering glycols from used glycol-containing technical fluids, especially from used antifreeze.
Large amounts of antifreeze are used. After use, it may contain, in addition to water, up to 50% by weight of glycols, especially ethylene glycol and propylene glycol, and specific additives, but also, according to origin and field of use, specific contaminants. Other glycol-containing technical fluids may contain, in addition to water, up to 90% by weight of glycols. For this reason used antifreeze must not simply be allowed to pass into the environment, but has to be specially disposed of or else recycled.
Further, large amounts of liquids containing glycol, especially ethylene glycol, are obtained in the manufacture of polyesters, especially polyester fibers; these liquids also contain, in addition to water, other impurities stemming from the process.
In the case of recycling, the chief concern is to recover the glycol components, especially ethylene glycol. Recovering the additive components as well as specific contaminants does not make technical sense because of their multitude and variety. But it is specifically these ingredients which, because of their physical and chemical properties, can appreciably hinder or impair the recovery of the glycols from the used antifreeze.
A number of methods have been developed for removing the glycols from the used antifreeze by simple distillation at atmospheric pressure or reduced pressure, as described for example in DE-A-40 30 331.
In principle, distillation is the processing method of choice. However, it is always associated with the imposition on the material being processed of a certain thermal stress, which causes the actual problems.
The abovementioned additives are usually organic and inorganic solids which, on distillation, will gradually accumulate in the bottom product and settle out. This gives rise to clumping, encrustation and caking in the heated parts of the distillation plant. This is the case even when, instead of a simple batch distillation, a thin-film or falling-film evaporator is used.
In consequence, the high thermal stress gives rise to decomposition reactions whose products reappear in the glycol distillate and have an adverse effect on its properties even in trace amount.
For instance, the inorganic nitrites frequently present in antifreeze as corrosion inhibitors can combine with organic nitrogen compounds to form nitrosamines. For this reason the distillation of the used antifreeze should be preceded by a reduction of the nitrites. Since the known methods for reducing nitrites almost all operate in an acid medium, but antifreeze is at best neutral or usually even alkaline, complete reduction requires the addition of an acid. The attendant salt formation additionally worsens the above-described situation of the distillation.
The intrinsically actually very effective way of getting rid of the nitrosamines by boiling in a strongly alkaline medium is not advisable because of the known safety risks of concentrating glycol bottoms.
The other additives and the contaminants from the use of the antifreeze, too, interfere with the used antifreeze processing and glycol recovery. Used antifreeze, for example from the automotive sector, contains, as a consequence of its use, contaminants such as solids through abrasion of metals and sealing materials, and also mineral oil and lubricant constituents. Lack of care in collecting the used antifreeze, however, may also mean that, for example, paint residues, cleaners and-used oils are present as contaminants.
Altogether these components have a color—but especially also an odor-conferring effect on the recovered glycols—and the higher the processing temperature, the greater the effect.
Virtually all recycled glycols have a more or less pronounced, very typical and usually very unpleasant odor.
It is an object of the present invention to provide a recycling process which is free of the above-described problems and which yields pure, colorless and odorless glycol recyclate in as simple a manner as possible.
We have found that this object is achieved by a process for recovering glycols from used glycol-containing technical fluids, especially from used antifreeze, which comprises adding to the used glycol-containing technical fluids an organic solvent which forms with the glycols to be separated off an azeotropic mixture which has a lower boiling point than the glycol itself and distilling off this azeotropic mixture.
Of particular suitability are those azeotropes which, on the one hand, have an atmospheric pressure boiling point which is not too high, i.e. still distinctly below the boiling point of glycols themselves, and, on the other, contain high glycol contents and which have miscibility gaps, in particular at low temperatures.
Organic solvents which form binary azeotropic mixtures with glycols, especially with ethylene glycol, include in particular toluene, o-chlorotoluene, o-bromotoluene, styrene, o-toluidine, n-octanol, 1,2-dibromo-ethane, 1,
2
-dibromobutane, amyl acetate and dichloromethane.
In principle, the azeotropic mixtures can also be distilled off at subatmosphere pressure to lower the boiling points, thus working under milder conditions and using less energy.
An extremely suitable organic solvent is pseudocumene (1,2,4-trimethylbenzene), which has a particularly high proportion of ethylene glycol in the azeotrope.
However, the best results are obtained with xylenes; it is customary to use the technical grade mixture of o-, m- and p-xylene. For instance, xylenes and ethylene glycol form azeotropic mixtures having glycol contents from 15 to 20% by weight and boiling at from 130 to 140° C. At room temperature, the mixtures separate into two phases. Glycol can therefore be continuously separated off. The xylenes are recirculated for continuous entrainment, so that comparatively little entraining agent is needed for the gentle processing of large quantities of glycol.
It is also possible to use mixtures of the organic solvents mentioned, for example to form ternary azeotropic mixtures.
The glycols to be recovered from the used antifreeze include ethylene glycol as main component or even as almost the sole component; in addition propylene glycol, diethylene glycol, triethylene glycol, dipropylene glycol, 1,3-butylene glycol and hexylene glycol (2-methyl-2,4-pentandiol) as examples of higher glycols may be found.
The used technical fluids mentioned normally include 10% by weight or more of water, especially 50% by weight or more of water with antifreeze, the bulk of which should preferably be removed by distillation prior to glycol recovery. The distillative removal of water is carried out either by concentrating under reduced pressure and hence at temperatures where the thermal stress is only small; or else by likewise separating off the water by azeotropic entrainment, advantageously with the same solvent or the same solvent mixture as also used for entraining the glycol.
During the azeotropic entrainment of glycols, the additives and specific contaminants present in the used technical fluids gradually separate out, but do not clump or cake; stirring is possible, if necessary. In fact, these ingredients are obtained as a readily stirrable and pumpable but also filterable suspension in the particular entrainer. Nor is there any interference here from subsequently added components, for example alkali metal hydroxides added for avoiding nitrosamine formation in antifreeze or for hydrolyzing dialkyl terephthalates as an example.
The glycol phase isolated in this way does already largely consist of the product of value and additionally contains at most only traces of the entrainer, which can be removed by simple means (stripping or distillation). The entrainer can be freed of the precipitated additives by filtration or, by addition of water to dissolve the additives and removal of the aqueous phase, recovered and re-used.
The process of the present invention yields pure, colorless and in particular odorless recovered
Balzer Wolf-Dieter
Mohr Jurgen
BASF - Aktiengesellschaft
Manoharan Virginia
Oblon & Spivak, McClelland, Maier & Neustadt P.C.
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