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Catalytic Dewaxing
Although included under the separation processes, catalytic dewaxing is actually a low-severity conversion process involving a selective catalytic cracking of n-paraffins. Because of removing wax (long chain n-paraffins) by chemical reaction, the process is called dewaxing. The selective cracking of n-alkanes takes place in the pores of molecular sieve catalysts (zeolites) with pore openings in the order of 0.6nm, which keep i-paraffins out because of their larger size due to branching in the hydrocarbon skeleton, as shown in Figure 5.13. This selective cracking increases the ratio of i-paraffins to n-paraffins in the product and lowers its pour point. Hydrogen is introduced along with the feed to prevent coking on the catalyst surfaces (Figure 5.14). The cracking of n-paraffins produces distillate fuels such as gasoline as a by-product from catalytic dewaxing.
The advantages of catalytic dewaxing include [3]:
- production of lube base stock with lower pour point and in higher yield compared to the product obtained from solvent dewaxing. Low yield from solvent dewaxing results from the difficulty of separating the oil from the wax;
- lower capital investment;
- good product stability;
- flexibility to produce both lube oil base stock and light distillates.
![see text for more detail, shows molecular sieve that i-alkanes can't get in](/fsc432/sites/www.e-education.psu.edu.fsc432/files/Lesson5/Lesson5Fig13.png)
![Catalytic dewaxing process. See text above for more info.](/fsc432/sites/www.e-education.psu.edu.fsc432/files/Lesson5/Lesson5Fig14.png)
Image Reads:
Catalytic cracking of long straight chains into shorter chains
-Remove wax chemically
-cracking creates free radicals
-to prevent the formation of coke, add hydrogen to prevent disproportionation
The image also includes a simplified diagram:
DAO enters a heater with hydrogen gas present, then it goes into a reactor, 280°-400°C, at 300-1500 psi. In the reactor, there is a catalyst – a molecular sieve, a zeolite (e.g. mordenite). From there it goes to distillation which separates naphtha (becomes gasoline) and lube oil base stock.
[3] Petroleum Refining, by J. H. Gary, G. E. Handwerk, M. J. Kaiser, 5th Edition, CRC Press NY, 2007, Chapter 15, pp.321-322.