Appeal No. 2004-0495 Paper 22 Application No. 09/503,599 Page 3 transesterification catalyst, including organic and inorganic compounds of titanium, lanthanum, zinc and cobalt, is mixed with 1,3-propanediol prior to mixing with the terephthalic acid ester (3:9-28). Still further according to the specification, the preheated 1,3-propanediol/terephthalic acid ester mixture may be injected into the ester exchange vessel at or below about the midpoint of the vessel (4:34 - 5:1). For example, a mixture of preheated, catalyzed 1,3-propanediol and preheated dimethylterephthalate is injected into the base of the exchanger, and additional virgin 1,3-propanediol, typically at ambient temperature, is injected at the quarterpoint of the exchange column. In this embodiment, the mixture that is injected into the base of the exchanger has a lower mole ratio of 1,3-propanediol to dimethylterephthalate and a higher catalyst concentration ..., such that the overall mole ratio and catalyst concentration remain within the above-described ranges, after taking into account the additional 1,3-propanediol that is injected at the quarter point. In still another alternative, preheated dimethylterephthalate and preheated catalyzed 1,3-propanediol are injected into the exchanger separately without premixing. For example, the dimethylterephthalate is injected into the base of the exchanger, and the catalyzed 1,3-propanediol is injected at the quarterpoint. [Specification, 5:18-31.] Gaseous reaction products typically include methanol vapor, acrolein and allyl alcohol, while liquid reaction products include bis(3-hydroxypropyl) terephthalate monomer, low molecular weight oligomers of 1,3-propanediol and terephthalic acid, and less than 9 wt.% unreacted terephthalic acid ester (id., 6:4-23). We make reference to appellants' Appeal Brief ("Brief," Paper 19, filed 11 March 2003) and the Examiner's Answer ("Answer," Paper 20, mailed 3 April 2003). The examiner relies on the following references in his rejection. Armstrong et al. (Armstrong) 3,534,082 13 October 1970 Kurian et al. (Kurian) 5,840,957 24 November 1998Page: Previous 1 2 3 4 5 6 7 8 9 10 11 NextLast modified: November 3, 2007