Method of recovery of terephthalic acid and ethylene glycol...

Organic compounds -- part of the class 532-570 series – Organic compounds – Carboxylic acids and salts thereof

Reexamination Certificate

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C562S483000, C562S485000

Reexamination Certificate

active

06239310

ABSTRACT:

Subject of the invention is the method of recovery of terephtalic acid and ethylene glycol from poly/ethylene terephtalate/ waste.
Still growing global production of poly/ethylene terephtalate/, which is used as a popular material for the production of bottles and containers, industrial shapes, synthetic fibres, insulation foils and other everyday use articles, causes, besides its numerous utility values, a fast increase of its wastes amount.
The chemical nature of poly/ethylene terephtalate/ causes that as a plastic of an extraordinary high resistance against the extremely severe atmospheric conditions, the wastes do not yield to microbiological degradation and a natural decomposition and they last, occupying in the unchanged form and being very noxious and durable pollution of the environment.
At the same time the raw materials for a production of poly/ethylene terephtalate/, i.e. ethylene glycol and terephtalic acid are still expensive.
The manufacture of poly/ethylene terephtalate/ waste for the regranulate, which is then added to the principal raw material in a process of forming any products does not solve the waste problem and similarly, as its harmful combustion, it is a stopgap.
Till now, from the American patent description no. 4.542239 a process of recovery terephtalic acid from poly/ethylene terephtalate/ is known, which is based on a reaction of suitably disintegrated wastes, comprising used containers and bottles of beverages, with a medium, containing ammonium hydroxide at the increased temperature and an increased pressure, and then the acidification of formed aqueous solution of water-soluble diammonium salt of terephtalic acid to precipitate terephtalic acid. A part of the solution remained after separation of terephtalic acid was subjected to the treatment with alkaline medium to separate ammonium, which was recycled together with a second part of the solution, remained after separation of terephtalic acid, as the charge material in a consequent part of substrates.
From the German patent application no. 19629042.2 a method of production terephtalic acid and ethylene glycol from poly/ethylene terephtalate/ waste is known. The process is carried in a slightly alkaline medium of carbonates of the I-st group metals or ammonium carbonate, by the decreased pH value, which does not allow any undesired side reactions and prevents the contamination of products.
In a known method suitably disintegrated poly/ethylene terephtalate/ wastes are subjected to the operation of an aqueous solution of alkali metal or ammonia carbonate while the temperature is increased gradually, preferably up to 200° C., and then the temperature is kept constant till the digestion of polyester is completed. Carbon dioxide, formed during the reaction is permanently carried away from the reaction environment under a constant pressure and is absorbed in an aqueous solution of alkali metal hydroxide, preferably of sodium Na, potassium K or ammonia water till the saturation moment. A reaction mixture, after separation of solid impurities and cooling, is then subjected to an oxidation process, preferably in aqueous solution of hydrogen peroxide of a concentration of 3% b.w., and then the solution is neutralised with an acid solution, preferably mineral acid solution, till the precipitation of terephtalic acid is completed. From a resulted suspension of terephtalic acid in a solution of ethylene glycol and salt of an acid used for the neutralisation a solid phase is separated, which is then subjected to the purification process, including washing and/or crystallisation and drying, which gives in a result terephtalic acid of a desired water content. Ethylene glycol is distilled off from the resulted solution, after evaporation of water and separation the salt of an acid used for neutralisation. Carbonate, formed in a result of absorption of educed carbon dioxide in hydroxide or ammonia solution is then used in a consequent batch, processed according to the known method.
In the method according to the invention, disintegrated poly/ethylene terephtalate/ wastes are heated with a reagent substance, chosen from the group, comprising bicarbonates of ammonia and alkali metals, ammonium carbamate and urea, which substances are used in an aqueous solution in amounts not less than a stechiometric amount at a temperature between 150°-280° C.
After the poly/ethylene terephtalate/ is digested a resulted aqueous solution of terephtalic acid salts is subjected to the further processing according to a method known from the German patent application no. 19629042.2, comprising filtering of a hot solution, neutralisation of a filtrate with a mineral acid, separation of terephtalic acid, washing of terephtalic acid with water and the eventual crystallisation from water, a neutralisation resulted filtrate and separation of ethylene glycol using distillation or extraction.
The preferable course of the reaction carried using a method according to the invention results at the temperatures range between 180-200° C.
The method according to the invention enables a production of high purity products demanded by the market and it gives a possibility of utilisation of wastes, being the durable and noxious pollution of a natural environment.


REFERENCES:
patent: 5545746 (1996-08-01), Benzaria et al.
patent: 839371 (1960-06-01), None
patent: 163385 (1988-09-01), None

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