Organic compounds -- part of the class 532-570 series – Organic compounds – Carboxylic acids and salts thereof
Reexamination Certificate
2002-09-13
2003-11-18
Rotman, Alan L. (Department: 1625)
Organic compounds -- part of the class 532-570 series
Organic compounds
Carboxylic acids and salts thereof
C568S858000
Reexamination Certificate
active
06649792
ABSTRACT:
FIELD OF THE INVENTION
The invention relates to the method of chemical recycling of polyethylene terephthalate waste to terephtalic acid and ethylene glycol.
BACKGROUND OF THE INVENTION
The polycondensation of ethylene glycol, in combination with terephthalic acid, to polyethylene terephthalate (PET) is a reversible reaction process, which makes it possible to de-polymerize PET back to monomers or oligomers. Essentially, PET de-polymerizing can be conducted in the same manner as glycolysis, hydrolysis or alcoholysis. The decomposition of PET in glycolic environment, i.e. glycolysis, is in principle based on the transesterification of the PET glycol, resulting in a mixture of aromatic polyols, which can be processed in the production of polyurethanes, or unsaturated polyester resins (U.S. Pat. Nos. 3,222,299, 4,078,143). When the input raw material for the glycolysis-type method of recycling PET waste is sufficiently pure, i.e. sorted out, washed and without admixtures of chromatic PET, the oligomeric products of this process can be used for polymerizing the new PET.
The monomers usable for polycondensation back to PET can be obtained through the process of hydrolysis or alcoholysis of PET waste. The products of PET hydrolysis include ethylene glycol and terephthalic acid, while alcoholysis results in ethylene glycol and respective esters of the terephthalic acid. The older process patented by the DuPont company (U.S. Pat. No. 3,544,622) is based on the hydrolysis of crushed PET in aqueous solution of NaOH and ethyleneglycol, at a temperature ranging from 90 to 1500 Centigrade and under atmospheric pressure, to disodium salt of terephthalic acid. The yield of disodium salt of terephthalic acid. The yield of disodium salt of terephthalic acid is 97.5%. The process developed later by the Michigan University of Technology for processing waste bottles is based on the hydrolysis of crushed PET in a surplus of water, at a temperature of from 150 to 2500 Centigrade and under increased pressure, catalyzed by sodium acetate (U.S. Pat. No. 4,542,239). Through this process, the complete decomposition of PET to ethyleneglycol and terephthalic acid is achieved within 4 hours.
A different process of neutral hydrolysis of condensation polymers is subject to U.S. Pat. No. 4,605,762. This invention essentially consists in neutral hydrolysis of condensation polymers by superheated steam. According to this invention, polyester-, polyamide- or polycarbonate based waste can be used as the input materials for this process. The hydrolytic process is conducted continuous in a pressure hydrolytic reactor at a temperature between 200 and 300° Centigrade and under pressure of minimally 1.5 MPa. The process is designed as counter-current, with the steam supplied to the bottom part of the reactor and the solution of the condensate hydrolysis product trapped in and drawn off from the reactor upper part. The thermal energy of the supplied steam is used to heat up the reactor. The input polymeric material can be pre-processed in a screw extruder and enter the hydrolytic reactor in the form of melt.
According to another invention (U.S. Pat. No. 6,031,128), terephthalic acid can be produced from PET waste using alkaline hydrolysis by waste water from the process of chromatic polyester fiber treatment. This water contains alkaline hydroxide and wetting agents.
Further inventions, mainly those of later date, concern procedures resulting in higher purity of the final product, i.e. the terephthalic acid. According to WO 95/10499, the process essentially consists in alkaline hydrolytic de-polymerization of the input polyester material. This process is improved by including an oxidation phase, preferably aeration, thus converting soluble contaminating components to insoluble ones. The insoluble oxidation products of the contaminants are subsequently removed by means of filtration. The hydrolysis stage can be further improved by adding a non-ionogenic wetting agent and quaternary ammonium hydroxide to the hydrolyzed mixture.
The process according to WO 97/24310 tackles the manner of regenerating high-purity terephthalic acid from a raw material based on PET waste. It uses alkaline hydrolysis by aqueous solution of alkaline hydroxide or alkaline earth metal hydroxide in combination with a wetting agent. Terephthalic acid is obtained from the hydrolyzate by means of its acid neutralization. Higher purity of the precipitated terephthalic acid is in this case achieved by means of controlled enlargement of the terephthalic acid particles through its crystallization.
The method of crushed PET decomposition under the effect of different alcohols was patented by Eastman Kodak in 1970 (U.S. Pat. No. 3501420). The best-suitable alcohol for PET decomposition however appears to be methanol. The methanolytic process is relatively tolerant to contamination of the input material. Chromatic PET types are no obstacle to obtaining products which are suitable for clear polymer synthesis of top quality. During a typical process of methanolysis, PET melt is mixed with methanol in a 1:4 ratio, and the mixture is heated to a temperature between 160 and 240° Centigrade under pressure of 2.0 to 7.0 MPa for a period of approximately one hour. A yield of 99% of dimethylterephthalate is reported (U.S. Pat. No. 3,403,115).
An advantage of processes based on glycolysis are relatively low investment costs, but in order to obtain raw material suitable for the polymerization of new PET, the input PET waste material needs to be highly pure and without admixtures of chromatic PET types. PET alcoholysis, on the other hand, and particularly methanolysis, while relatively tolerant to the contents of impurities in the input material, require very high investments into the necessary technological equipment.
SUMMARY OF THE INVENTION
The above-mentioned disadvantages of the actual state of technology are to a great extent eliminated by the method of chemical recycling of polyethylene terephthalate waste to terephthalic acid and ethylene glycol, as the hydrolysis of polyethylene terephthalate waste with the purpose of its de-polymerization is based, according to this invention, on crushed discarded and unsorted polyethylene terephthalate products, especially drink bottles which contain a maximum of 30% of contaminants. Essentially the process includes the following steps:
a) The first step involves separation of the polyethylene terephthalate component of the input material by its conversion to brittle form by means of crystallization, grinding and subsequent sifting. In keeping with the invention, the polyethylene terephthalate crystallization is carried out by tempering the input material to a temperature in the range of 140 to 190° Centigrade for a period of at least 25 and at most 60 minutes. The essence of the purification of the input material in this manner is the separation of the polyethylene terephthalate component, which is capable under such conditions of crystallization accompanied by its embrittlement, from the contaminants in the input mixture such as polyolefins, PVC, paper and adhesive residues which stay tough under the described conditions and resist the subsequent grinding. The ground mixture then contains fine-grained particles of polyethylene terephthalate and very coarse-grained particles of the contaminants. The ratio between medium-sized particles of the polyethylene terephthalate component and medium-sized particles of other components of the ground material is approximately 1:10. The polyethylene terephthalate component is subsequently removed from this mixture by sifting.
b) The next step consists of continuous two-stage hydrolysis of the polyethylene terephthalate, conducted in the first stage by feeding steam to the polymer melt in the extrusion reactor. The reactor is composed of a double-screw extruder, with the length of the screws representing at least 25-times their diameter (L/D≧25), and a follow-up static mixer at its outlet. The products of the first stage of hydrolysis are carried away from the extrusion reactor outle
Jirou{haeck over (s)}ek Jaroslav
{haeck over (S)}irek Milan
Dykema Gossett PLLC
Oh Taylor V
Rotman Alan L.
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