Moulded insulation bodies
Moulded insulation bodies, processes for the production thereof and use thereof consisting essentially of ceramic material comprising SiO 2 fibers and Al 2 O 3 fibers which has been produced using Al 2 O 3 sol as a binder and kilned at a temperature of above 800° C. for insulation of the ends of cracking tubes of a tubular reactor for performing a steam reforming process for generating synthesis gas which project out of the reactor heating space.
1. A cracking tube for use in a tubular reactor, the cracking tube comprising a top portion configured to be at least partially disposed above a ceiling of the tubular reactor, a bottom portion configured to be at least partially disposed below a floor of the tubular reactor, and a middle portion configured to be disposed within a heating space of the tubular reactor, wherein the cracking tube further comprises:
a catalyst bed disposed in the middle portion, wherein the catalyst bed is configured to convert a reactant gas stream comprising hydrocarbons and steam into synthesis gas,
a first internal molded insulation body disposed in the top portion of the cracking tube, wherein the first internal molded insulation body is produced from a ceramic material comprising SiO 2 fibers and Al 2 O 3 fibers using a process comprising the steps of:
a. providing a flowable mixture comprising SiO 2 fibers and Al 2 O 3 fibers and a binder comprised of an Al 2 O 3 sol;
b. producing a preform by filling the flowable mixture into a hollow mold;
c. kilning the preform at a temperature of at least 800° C.; and
a second internal molded insulation body disposed in the bottom portion of the cracking tube.
2. A cracking tube for use in a tubular reactor, the cracking tube comprising a top portion configured to be at least partially disposed above a ceiling of the tubular reactor, a bottom portion configured to be at least partially disposed below a floor of the tubular reactor, and a middle portion configured to be disposed within a heating space of the tubular reactor, wherein the cracking tube further comprises:
a catalyst bed disposed in the middle portion, wherein the catalyst bed is configured to convert a reactant gas stream comprising hydrocarbons and steam into synthesis gas,
an internal molded insulation body disposed in a portion of the cracking tube selected from the group consisting of the top portion, the bottom portion, and combinations thereof, wherein the internal molded insulation body is produced from a ceramic material comprising SiO 2 fibers and Al 2 O 3 fibers using a process comprising the steps of:
a. providing a flowable mixture comprising SiO 2 fibers and Al 2 O 3 fibers and a binder comprised of an Al 2 O 3 sol;
b. producing a preform by filling the flowable mixture into a hollow mold;
and
c. kilning the preform at a temperature of at least 800° C.; and
an inlet for reactants and an outlet for products, wherein the inlet and the outlet are disposed within a section of the cracking tube selected from the group consisting of the top portion, the bottom portion, and combinations thereof.
3. The cracking tube according to claim 2 , wherein the inlet and the outlet are arranged at opposite ends of the cracking tube which project out of the heating space of the tubular reactor.
4. The cracking tube according to claim 2 , wherein the inlet and the outlet are arranged at a same end of the cracking tube which projects out of the heating space of the tubular reactor and in that at an opposite end of the cracking tube a free interior space is present which serves to deflect a gas flow leaving the catalyst bed into a heat exchanger tube arranged inside the catalyst bed.
5. The cracking tube according to claim 2 , wherein the molded insulation body has a circular arc profile.
6. The cracking tube according to claim 2 , wherein the molded insulation body is in a shape selected from the group consisting of a half shell, a quarter shell, and cylindrical.
7. A process for performing a steam reforming process for generating synthesis gas, the process comprising the steps of:
providing a tubular reactor having the cracking tube as claimed in claim 2 ;
flowing a reactant gas comprising hydrocarbons and steam into an inlet of the cracking tube to generate the synthesis gas; and
collecting the synthesis gas from an outlet of the cracking tube.
8. The process according to claim 7 , wherein the inlet and the outlet are arranged at opposite ends of the cracking tube which project out of a heating space of the tubular reactor.
9. The process according to claim 7 , wherein the inlet and the outlet are arranged at a same end of the cracking tube which projects out of the heating space of the tubular reactor and in that at an opposite end of the cracking tube a free interior space is present which serves to deflect the gas flow leaving the catalyst bed into a heat exchanger tube arranged inside the catalyst bed.
10. The process according to claim 7 , wherein the molded insulation body has a circular arc profile.
11. The process according to claim 7 , wherein the molded insulation body is in a shape selected from the group consisting of a half shell, a quarter shell, and cylindrical.