Process for the preparation of methane and/or ethane
AssigneeShell Oil Company
InventorNigel Wagstaff
Life of this patent
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Abstract
A process for the production of methane and ethane from a C.sub.2 -C.sub.4 paraffins hydrocarbon feed stream of higher average carbon number than the product which comprises contacting said feed with certain crystalline silicates at an elevated temperature and a pressure above 10 bar.
Claims9
A process for the preparation of methane and/or ethane, which comprises contacting as feed a C.sub.2-4 paraffin or a hydrocarbon mixture which consists of more than 75% C.sub.2-4 paraffins and which C.sub.2-4 paraffins have an average molar carbon number which is at least 0.5 higher than that of the C.sub.2.sup.- paraffin fraction of the product, at an elevated temperature of from 400.degree. to 800.degree. C., a pressure of above 10 to below 100 bar, and a space velocity of from 0.1 to 20 g.g.sup.-1.h.sup.-1 in a contact zone with a crystalline silicate as the catalyst, which silicate is characterized in that after 1 hour's calcining in air at 500.degree. C. it has the following properties:
- (a) thermally stable up to a temperature above 600.degree. C.,
- (b) an X-ray powder diffraction pattern showing, inter alia, the reflections give in Table A.
- TABLE A ______________________________________ Radiation :
- Cu--K Wavelength 0.15418 nm 2 .theta. relative intensity ______________________________________ 7.8-8.2 S 8.7-9.1 M 11.8-12.1 W 12.4-12.7 W 14.6-14.9 W 15.4-15.7 W 15.8-16.1 W 17.6-17.9 W 19.2-19.5 W 20.2-20.6 W 20.7-21.1 W 23.1-23.4 VS 23.8-24.1 VS 24.2-24.8 S 29.7-30.1 M ______________________________________
- wherein the letters used have the following meanings:
- VS=very strong;
- S=strong;
- M=moderate;
- W=weak;
- .theta.=angle according to Bragg.
- (c) after conversion of the silicate into the H-form and after evacuation at 2.times.10.sup.-9 bar and 400.degree. C. for 16 hours and measured at a hydrocarbon pressure of 8.times.10.sup.-2 bar and 100.degree. C. the adsorption of n-hexane is at least 0.8 mmol/g, the adsorption of 2,2-dimethylbutane at least 0.5 mmol/g and the ratio ##EQU3## (d) the composition, expressed in moles of the oxides, is as follows:
- y.(1.0.+-.0.3)M.sub.n/.sbsb.2 O.y.Al.sub.2 O.sub.3.SiO.sub.2
- wherein M=H and/or alkali metal and/or alkaline-earth metal, n is the valency of M and y.gtoreq.0.01;
- and withdrawing a methane and ethane containing product from said catalyst zone.
Dependencies are inferred from the claim text.