Method and reactor for cracking hydrocarbon
A method for cracking hydrocarbon, comprises: providing steam and hydrocarbon; and feeding steam and hydrocarbon into a reactor accessible to hydrocarbon and comprising a perovskite material of formula A a B b C c D d O 3-δ , wherein 0<a<1.2, 0≦b≦1.2, 0.9<a+b≦1.2, 0<c<1.2, 0≦d≦1.2, 0.9<c+d≦1.2, −0.5<δ<0.5; A is selected from calcium, strontium, barium, and any combination thereof; B is selected from lithium, sodium, potassium, rubidium and any combination thereof; C is selected from cerium, zirconium, antimony, praseodymium, titanium, chromium, manganese, ferrum, cobalt, nickel, gallium, tin, terbium and any combination thereof; and D is selected from lanthanum, cerium, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, ebium, thulium, ytterbium, lutetium, scandium, titanium, vanadium, chromium, manganese, ferrum, cobalt, nickel, copper, zinc, yttrium, zirconium, niobium, molybdenum, technetium, ruthenium, rhodium, palladium, silver, cadmium, hafnium, tantalum, tungsten, rhenium, osmium, iridium, platinum, gold, gallium, indium, tin, antimony and any combination thereof.
1. A method of inhibiting coke deposit formation in a hydrocarbon cracking reactor having an inner surface accessible to said hydrocarbon and wherein a hydrocarbon comprising ethane is cracked in the presence of steam at a temperature of about 480° C. to about 870° C. to form ethylene, said inner surface comprising a perovskite material selected from the group consisting of BaZr 0.3 Ce 0.7 O 3 , BaZr 0.7 Ce 0.3 O 3 , and BaCe 0.5 Zr 0.5 O 3 and combinations thereof whereby said perovskite gasifies said coke to produce CO, CO 2 , and hydrogen.
2. A method as recited in claim 1 wherein said perovskite material is applied to said interior surfaces as a coating.
3. A method as recited in claim 1 wherein said perovskite material is present in the form of a pressed powder.
4. A method as recited in claim 1 wherein said inner surface is devoid of Ni.
5. A method as recited in claim 1 wherein the perovskite material is BaZr 0.7 Ce 0.3 O 3 .
6. A method as recited in claim 1 wherein the perovskite material is BaCe 0.5 Zr 0.5 O 3 .
7. The method of claim 1 , being operated at a temperature in a range from about 700° C. to about 870° C. and wherein a weight ratio of steam to hydrocarbon is in a range from about 3:7 to about 7:3.
8. The method of claim 1 , being operated at a temperature in a range from about 480 to about 600° C., and a weight percentage of the steam in the steam and hydrocarbon is about 1 wt % to about 2 wt %.
9. The method of claim 1 , wherein the perovskite material is BaZr 0.3 Ce 0.7 O 3 .