Autothermic reactor and process using oxygen ion--conducting dense ceramic membrane

• US 5,980,840 A
• Filed: 04/25/1997
• Issued: 11/09/1999
• Est. Priority Date: 04/25/1997
• Status: Expired due to Fees

• Current Assignee: BP Amoco (BP PLC)
• Original Assignee: BP Amoco (BP PLC)
• Inventors: Bhattacharyya, Alakananda, Kleefisch, Mark S., Udovich, Carl A., Kobylinski, Thaddeus P.
• Primary Examiner(s): Warden, Sr., Robert J.
• Assistant Examiner(s): KENNEDY, JAMES C
• Application Number:
  US08/845,310
• Time in Patent Office: 928 Days
• Field of Search: 422/191, 422/211, 422/238, 422/239, 422/204, 204/410, 204/265, 204/421, 429/8, 429/30, 48/198.7, 48/127.7, 95/54
• US Class Current: 422/211
• CPC Class Codes: B01D 53/885 Devices in general for catalytic purification of waste gases
• CPC Class Codes: B01J 19/2475 Membrane reactors
• CPC Class Codes: B01J 2219/00117 with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction
• CPC Class Codes: B01J 2219/00135 Electric resistance heaters
• CPC Class Codes: B01J 2219/00164 controlling the flow
• CPC Class Codes: B01J 2219/00166 controlling the residence time inside the reactor vessel
• CPC Class Codes: B01J 8/009 Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
• CPC Class Codes: C01B 2203/1052 Nickel or cobalt catalysts
• CPC Class Codes: C01B 2203/1082 Composition of support materials
• CPC Class Codes: C01B 2203/142 At least two reforming, decomposition or partial oxidation steps in series
• CPC Class Codes: C01B 2203/82 Several process steps of C01B2203/02 - C01B2203/08 integrated into a single apparatus
• CPC Class Codes: C01B 3/382 Multi-step processes
• CPC Class Codes: C01B 3/40 characterised by the catalyst

Abstract

The present invention relates to devices for conducting, simultaneously, exothermic and endothermic chemical conversions with transfer of heat therebetween. More particularly, this invention relates to autothermic modules using oxygen ion-conducting dense ceramic membranes to separate, selectively, oxygen from an oxygen-containing gas and supply it directly to partial combustion of gaseous organic compounds. Processes using autothermic modules in accordance with this invention are, advantageously, used for production of synthesis gas comprising carbon monoxide and molecular hydrogen which synthesis gas is substantially free of deleterious and/or inert gaseous diluents such as nitrogen. In particular, for conversions, within the integral autothermic module, of natural gas or other forms of gaseous lower alkanes to synthesis gas by means of partial combustion followed by reforming.

Claims

1. A device for conducting, simultaneously, exothermic and endothermic chemical conversions, the device comprising a shell having an entrance port, an exit port and a passageway therebetween for flow of gases comprising a source of oxygen, and within the shell at least one autothermic module for chemical conversions, each module comprising a al combustion compartment having a feed port and a catalytic compartment containing a catalyst and having a product port, the catalytic compartment in flow communication with the partial combustion compartment, a wall of the partial combustion compartment and the passageway being coextensive and defined by a gas-tight partition at least a portion of which comprises a dense ceramic membrane, the dense ceramic membrane further comprising a crystalline mixed metal oxide which exhibits, at operating temperatures, electron conductivity, oxygen ion conductivity and ability to separate oxygen from a gaseous mixture containing oxygen and one or more other volatile components by means of the conductivities, and the catalytic compartment disposed within the partial combustion compartment such that at least a portion of a wall of the catalytic compartment is adjacently disposed to receive radiant heat from at least a portion of the gas-tight partition.

2. The device according to claim 1 wherein the crystalline mixed metal oxide composition is selected from a class of materials which have an X-ray identifiable crystalline structure based upon the structure of the mineral perovskite, CaTiO₃.

3. The device according to claim 1 wherein the crystalline mixed metal oxide composition represented by

4. The composition according to claim 3 wherein the integral crystalline structure comprises layers having a perovskite structure held apart by bridging layers having a different structure.

5. The device according to claim 1 wherein the crystalline mixed metal oxide composition represented by

6. The mixed metal oxide composition according to claim 5 wherein x is a number in a range from 0.1 to 0.8, y is a number in a range upward from 0.1 to about 0.5, and β

is a number in a range from about 0.1 to about 6, and wherein the integral crystalline structure comprises layers having a perovskite structure held apart by bridging layers having a different structure.

7. The device according to claim 1 wherein the crystalline mixed metal oxide composition represented by

8. The device according to claim 1 wherein the crystalline mixed metal oxide composition represented by

9. The device according to claim 8 wherein X is a number in a range from 0.1 to 0.8, Y is a number in a range upward from 0.1 to about 0.5, and β

is a number in a range from about 0.1 to about 6, and wherein the integral crystalline structure comprises layers having a perovskite structure held apart by bridging layers having a different structure.

10. The device according to claim 1 wherein the crystalline mixed metal oxide composition represented by

11. A process for preparation of synthesis gas which comprises:

(A) Providing a device comprising a shell having an entrance port, an exit port and a passageway therebetween for flow of gases comprising a source of oxygen, and within the shell at least one autothermic module for chemical conversions, module comprising a partial combustion compartment having a feed port and a catalytic compartment containing a catalyst and having a product port, the catalytic compartment in flow communication with the partial combustion compartment, a wall of the partial combustion compartment and the passageway being coextensive and defined by a gas-tight partition at least a portion of which comprises a dense ceramic membrane, the dense ceramic membrane further comprising a crystalline mixed metal oxide which exhibits, at operating temperatures, electron conductivity oxygen ion conductivity and ability to separate oxygen from a gaseous mixture containing oxygen and one or more other volatile components by means of the conductivities, and the catalytic compartment disposed within the partial combustion compartment such that at least a portion of a wall of the catalytic compartment is adjacently disposed to receive radiant heat from at least a portion of the gas-tight partition;

(B) Maintaining a relatively high oxygen partial pressure in the passageway by supplying a gaseous mixture comprising a source of oxygen thereto through the entrance port and expelling a depleted gaseous mixture from the passageway through the exit port;

(C) Maintaining a relatively low oxygen partial pressure in the combustion compartment by supplying a dioxygen-free gaseous feed comprising one or more hydrocarbyl compound to the autothermic module through the feed port of the oxidation compartment;

(D) Permitting oxygen to be transported through the membrane from the oxygen-containing gaseous mixture having a relatively high oxygen partial pressure into the gaseous composition having a relatively low oxygen partial pressure, and oxidizing from about 20 to about 40 percent of the hydrocarbyl compounds in the feed to obtain heat and form a resulting mixture comprising oxidation products and unconverted hydrocarbyl compounds;

(E) Contacting the resulting mixture with the chemical conversion catalyst in the catalytic compartment at temperatures in a range from about 500°

C. to about 1150°

C. to form synthesis gas comprising hydrogen and carbon monoxide; and

(F) Permitting heat to be transferred from the partial combustion compartment into the catalytic compartment through a wall of the catalytic compartment, and expelling the synthesis gas from the catalytic compartment through the product port.

12. The process for preparing synthesis gas according to claim 11 wherein the catalyst comprises a composition formed by heat treating under reforming conditions to temperatures in a range upward from at least about 400°

C., a catalyst precursor composition comprising at least one hydrotalcite-like compound having formula;

space="preserve" listing-type="equation">[M.sup.2+.sub.w Al.sup.3+.sub.(2-y) M.sup.3+.sub.y (OH).sub.2(w+2) ].sup.2+ (A.sup.n-.sub.2/n)·

m H.sub.2 O,

where M²⁺ is at least one metal ion having a valence of 2+selected from the group consisting of magnesium, chromium, manganese, iron, cobalt, nickel, copper and zinc ions;

M³⁺ is at least one metal ion having a valence of 3+selected from the group consisting of titanium, vanadium chromium, manganese, iron, cobalt, nickel, gallium, ruthenium, rhodium, lanthanum, cerium, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium and iridium ions;

w is a number in a range from about 2 to about 20;

y is a number in a range from about 0 to about 2;

A^n- is an anion having a negative charge of n; and

m is 0 or a positive number.

13. The process of claim 12 wherein M²⁺ is magnesium ions;

M³⁺ is at least one metal ion selected from the group consisting of rhodium and iron ions.

14. The process of claim 12 wherein M³⁺ is rhodium ions, w is about 4;

y is a number in a range from about 0.00001 to about 1.5.

15. The process of claim 12 wherein M³⁺ is iron ions, w is about 4;

y is a number in a range from about 0.00001 to about 1.5.

16. The process of claim 12 wherein M²⁺ is magnesium ions;

M³⁺ is at least rhodium and iron ions, and wherein A^n- is carbonate.

17. The process according to claim 11 wherein from about 25 to about 35 percent of the hydrocarbyl compounds in the feed are converted to oxidation products.

18. The process according to claim 11 wherein the hydrocarbyl compounds are selected from the group consisting of methane, ethane, and other hydrocarbon gases.

19. The process according to claim 11 wherein the autothermic module is at temperatures in a temperature range from about 750°

C. to about 1050°

C.

20. The process according to claim 11 wherein the crystalline mixed metal oxide composition represented by