Poly(ethylene terephthalate) (PET) represents a significant portion of the post-consumer waste stream in the United States. Almost half of produced PET is recycled. Recycled PET is primarily material available in forms such as chips produced from soda bottles which have been physically separated from other waste material, washed, and dried. Much of the post-consumer PET waste cannot be physically separated to obtain sufficiently pure PET for recycle as PET polymer, but can only be concentrated into a polyester-rich waste component. It is important to find varied and higher value uses for this polyester-rich waste available for recycle. Accordingly, an economical process to allow reuse of these materials as industrial chemicals is desirable. Sufficiently pure PET scrap can be melted and reformed without depolymerization as described in U.S. Pat. Nos. 5,225,130; and 5,248,041.
At least three polyester tertiary recycling technologies are known. PET materials can be reacted with methanol to produce dimethyl terephthalate. This process, methanolysis, is the subject of U.S. Pat. No. 4,163,860 (Hoppert); U.S. Pat. No. 4,578,502 (Cudmore); U.S. Pat. No. 5,051,528 (Naujokas); U.S. Pat. No. 5,298,530 (Gamble); U.S. Pat. No. 5,391,263 (Hepner); and U.S. Pat. No. 5,414,022 Toot, Jr.). PET can also be reacted with ethylene glycol as described in column 1 of U.S. Pat. No. 4,078,143 (Malik); this process, glycolysis, apparently does not depolymerize the polyester completely to monomers, and is claimed to be less costly than methanolysis. Hydrolysis of PET under high temperatures and pressures yields terephthalic acid and ethylene glycol. Purification of the resulting terephthalic acid is costly, and this process does not appear to be economically attractive.
Depolymerizion of polyester is the subject of U.S. Pat. No. 5,414,106 (Smith); U.S. Pat. No. 5,414,107 (Smith); and U.S. Pat. No. 5,502,239 (Smith).
The existing recycling techniques suffer from relatively high process costs or product purity issues in the applications intended. The physical separation techniques employed to obtain a highly purified polyester material from some food packaging wastes have been successful, however these techniques are not universally applicable. Thus many polyester-rich wastes cannot be economically recycled using the existing polyester recycling techniques. Dissolution of polyester from polyester-rich waste streams, followed by decomposition into compounds which are soluble in ethylene carbonate or propylene carbonate at ambient temperature, offers a means to convert polyester waste directly into useful industrial solvents or inputs into other chemical processes.
The existing recycling techniques suffer from relatively high process costs or product purity issues in the applications intended. The physical separation techniques employed to obtain a highly purified polyester material from some food packaging wastes have been successful, however these techniques are not universally applicable. Thus many polyester-rich wastes cannot be economically recycled using the existing polyester recycling techniques. Dissolution of polyester from polyester-rich waste streams, followed by decomposition into compounds which are soluble in ethylene carbonate or propylene carbonate at ambient temperature, offers a means to convert polyester waste directly into useful industrial solvents or inputs into other chemical processes.
This invention is directed to a process for decomposing the polyester component of post-consumer or post-industrial waste into compounds that are liquid at room temperature and are useful as solvents or as inputs for other chemical processes. This invention is particularly directed to a process for the decomposition of poly ethylene terephthalate).
A process for decomposition of polyester into compounds that are soluble in ethylene carbonate or propylene carbonate at ambient temperature is disclosed. The process of the present invention allows recycling of polyester directly into useful industrial chemicals which can be employed as components of industrial solvents for purposes such as paint and grease stripping.
U.S. Pat. No. 4,118,187 (Sidebotham) and U.S. Pat. No. 4,137,393 (Sidebotham) employ solvents to selectively dissolve polyester from assortments of commingled fibers as a means of recovering unaltered polyester polymer of sufficient purity for reuse in polyester fiber production. One of the solvents named in these patents is the cyclic ester, propylene carbonate. U.S. Pat. No. 5,554,657 (Brownscombe) teaches the use of ethylene carbonate and propylene carbonate as solvents for polyester in the temperature range of 190 degrees to 200 degrees Celsius in an intricate process to recover polyester from a mixed polymer waste while maintaining the polyester polymer in polymer form.
Cyclic esters have been unexpectedly found to decompose dissolved polyester as the temperature of the solution is increased above about 215 degrees Celsius. This decomposition is evidenced by substantial reduction in the proportion of dissolved polyester that is recovered as precipitated polyester polymer upon cooling of the solution.
Poly(ethylene terephthalate) has been observed to dissolve in propylene carbonate only at a temperature between about 190 and 200 degrees Celsius. No appreciable dissolution of fibers is observed below a temperature of about 180 degrees Celsius. It has been unexpectedly discovered that polyester dissolved in cyclic esters decomposes when the solution is heated above a temperature of about 215 degrees Celsius. Upon cooling of the solution to ambient temperature, little or not precipitation of polyester polymer occurs. The polyester has been decomposed into monomeric and oligomeric units soluble in the cyclic ester solvent at ambient temperature. Thus, polyester extracted from polyester-rich waste streams by selective dissolution in a cyclic ester such as propylene carbonate or ethylene carbonate can be easily and immediately converted into a component of an industrial solvent by subjecting the polyester solution to increased temperature.
Polyester can be extracted from a mixed polymer waste by known techniques for dissolution in cyclic esters, solid-liquid separation may be necessary after dissolution of polyester but before decomposition of dissolved polyester depending upon the other constituents of the mixed polymer waste. Solid-liquid separation performed after decomposition of polyester should always be performed to yield a solvent solution containing minimal suspended solids.
The preferred solvent for dissolution of poly(ethylene terephthalate) is propylene carbonate. Propylene carbonate is known to be useful as a component of industrial solvents. U.S. Patent Application 20030119686 (Machac, Jr.) describes the environmental and employee health and safety benefits to be realized by utilization of industrial solvents containing propylene carbonate as opposed to more volatile and toxic solvents. Employing polyester decomposition products as a significant component of industrial solvents also containing cyclic esters such as ethylene carbonate, propylene carbonate, butylene carbonate, and mixtures thereof, will reduce the cost of these solvent compositions and allow them to compete more easily with some of the traditional industrial solvents.
Further details regarding the invention are set forth in the non-limiting example which follows. EXAMPLE Poly(ethylene terephthalate) yarn was cut into approximately 3 inch lengths, weighed, and place into an Erlenmeyer flask. Propylene carbonate was added to the flask such that 25 grams of poly(ethylene terephthalate) was admixed with 100 grams of propylene carbonate.
The Erlenmeyer flask was heated with gentle stirring on a hot plate. The poly (ethylene terephthalate) yarn was observed to be unaffected when the temperature of the admixture reached 180 degrees Celsius, but it had disappeared by the time the admixture had reached a temperature of 200 degrees Celsius. The admixture was further heated to a temperature of 220 degrees Celsius and held at this temperature of 15 minutes.
After the admixture was cooled to room temperature, it was filtered and the filtrate was weighted. Only 1.2 grams of solids were found in the admixture, thus approximately 95% of the polyester had been decomposed into compounds soluble in the propylene carbonate at room temperature.
The present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof, and accordingly, reference should be made to the appended claims, rather than to the foregoing specification, as indicating the scope of the invention.