Claims
- 1. A process for manufacturing a dehydrated nickel-containing material which comprises:
- (1-A) Blending in an aqueous medium (i) about two molar parts of one or more divalent metal compound none of which is a salt and comprises Ni.sup.2+ ions, or Ni.sup.2+ ions and at least one other divalent metal ion selected from the group consisting of Mg.sup.2+, Cu.sup.2+, Co.sup.2+, Zn.sup.2+, Fe.sup.2+ and Mn.sup.2+ ions, (ii) about one molar part in sum of a trivalent compound which is not a salt and comprises at least Al.sup.3+ ions and optionally another selected from the group consisting of Ga.sup.3+, Ni.sup.3+, Co.sup.3+, Fe.sup.3+, Mn.sup.3+, Cr.sup.3+, V.sup.3+, Ti.sup.3+, La.sup.3+ and In.sup.3+ ions, and (iii) about one-half to about one molar part of a water soluble interstitial anion precursor, to produce a mixture;
- (1-B) Heating the mixture to a temperature in a range of about 50.degree. C. to about 100.degree. C. and maintaining the mixture at elevated temperature for at least about one hour to form an anionic layered mixed hydroxide;
- (1-C) Recovering the anionic layered mixed hydroxide from the mixture; and
- (1-D) Calcining the recovered layered mixed hydroxide for not less than about one hour at a temperature of about 450.degree. C. or hotter, to produce a dehydrated material.
- 2. The process of claim 1 wherein the water soluble interstitial anion precursor is carbonate.
- 3. The process of claim 1 further comprising heat treating, to a temperature of at least about 700.degree. C. under reforming conditions, the dehydrated material of step 1-D to produce an at least partially collapsed composition for use as a catalyst for reforming of a hydrocarbyl compound to prepare synthesis gas comprising a mixture of carbon monoxide and molecular hydrogen.
- 4. The process of claim 3 wherein the heat treating is carried out under reforming conditions, and the composition for use as a catalyst contains metal particles of about 1 nanometer to about 1000 nanometers in size and containing at least nickel in the zero oxidation state.
- 5. The process of claim 4 wherein the composition for use as a catalyst comprises (a) M.sup.2+ O, (b) M.sup.2+ Al.sub.2 O.sub.4 spinel and (c) a hybrid phase comprising (i) a M.sup.2+ O component and (ii) a M.sup.2+ Al.sub.2 O.sub.4 spinel component in the same catalyst crystallite and joined through an epitaxial interface, said epitaxial interface being an area in the crystallite where crystalline species of both components (i) and (ii) coexist and form a well defined interface, and wherein M.sup.2+ is Ni.sup.2+ or a mixture of Ni.sup.2+ plus another metal ion or plus other metal ions.
- 6. The process of claim 5 wherein M.sup.2+ is Ni.sup.2+, and the crystallites are about 5 nanometers to about 400 nanometers in size.
- 7. The process of claim 1 wherein the divalent metal compound comprises Ni.sup.2+ ions or mixture of Ni.sup.2+ ions and another divalent metal ion selected from the group consisting of Mg.sup.2+, Zn.sup.2+ and Cu.sup.2+ ions.
- 8. The process of claim 7 wherein the trivalent metal ions are Al.sup.3+ ions, and the water soluble interstitial anion precursor is carbonate.
- 9. The process of claim 1 wherein the divalent metal compounds comprises Ni.sup.2+ ions and Mg.sup.2+ ions, the trivalent metal ions are Al.sup.3+ ions, and the water soluble interstitial anion precursor is carbonate.
- 10. The process of claim 1 wherein the anionic layered mixed hydroxide is hydrotalcite-like compound having formula:
- �M.sup.2+.sub.(1-x) M.sub.x.sup.3+ (OH).sub.2 !.sup.x+ (A.sub.x/n.sup.n-).mH.sub.2 O,
- wherein M.sup.2+ is a metal ion having a valence of 2+ and is Ni.sup.2+ or a mixture of Ni.sup.2+ and another ion selected from the group consisting of Mg.sup.2+, Zn.sup.2+ and Cu.sup.2+ ; M.sup.3+ is at least one metal ion having a valence of 3+ and is at least Al.sup.3+ ; x is a number greater than about 0.25 to about 0.50; A.sup.n- is an anion having a negative charge n; and m is 0 or a positive number.
- 11. The process of claim 10 further comprising heat treating, to a temperature in the range of about 800.degree. C. to about 1050.degree. C. under reforming conditions, the dehydrated material of step 1-D to produce an at least partially collapsed composition for use as a catalyst for reforming of a hydrocarbyl compound to prepare synthesis gas comprising a mixture of carbon monoxide and molecular hydrogen, wherein the catalyst comprises (a) M.sup.2+ O, (b) M.sup.2+ Al.sub.2 O.sub.4 spinel and (c) a hybrid phase comprising (i) a M.sup.2+ O component and (ii) a M.sup.2+ Al.sub.2 O.sub.4 spinel component in the same catalyst crystallite and joined through an epitaxial interface, said epitaxial interface being an area in the crystallite where crystalline species of both components (i) and (ii) coexist and form a well defined interface, and wherein M.sup.2+ is Ni.sup.2+ or a mixture of Ni.sup.2+ plus another metal ion or plus other metal ions.
- 12. A composition formed by heat treating to a temperature of at least about 700.degree. C. under conditons for reforming of a hydrocarbyl compound to prepare synthesis gas comprising a mixture of carbon monoxide and molecular hydrogen, a dehydrated nickel-containing material manufactured by a process which comprises:
- (12-A) Blending in an aqueous medium (i) about two molar parts of one or more divalent metal compound none of which is a salt and comprises Ni.sup.2+ ions, or Ni.sup.2+ ions and another divalent metal ion selected from the group consisting of Mg.sup.2+, Zn.sup.2+ and Cu.sup.2+ ions, and (ii) about one molar part in sum of a trivalent compound which is not a salt and comprises at least Al.sup.3+ ions and optionally another selected from the group consisting of Ga.sup.3+, Ni.sup.3+, Co.sup.3+, Fe.sup.3+, Mn.sup.3+, Cr.sup.3+, V.sup.3+, Ti.sup.3+, La.sup.3+ and In.sup.3+ ions, and (iii) about one-half to about one molar part of a water soluble interstitial anion precursor, to produce a mixture;
- (12-B) Heating the mixture to a temperature in a range of about 50.degree. C. to about 100.degree. C. and maintaining the mixture at elevated temperature for at least about one hour to form an anionic layered mixed hydroxide;
- (12-C) Recovering the anionic layered mixed hydroxide from the mixture; and
- (12-D) Calcining the recovered layered mixed hydroxide for not less than about one hour at a temperature of about 450.degree. C. or hotter, to produce a dehydrated nickel-containing material.
- 13. The composition of claim 12 wherein the water soluble interstitial anion precursor is carbonate.
- 14. The composition of claim 12 wherein the resulting compostion comprises (a) M.sup.2+ O, (b) M.sup.2+ Al.sub.2 O.sub.4 spinel and (c) a hybrid phase comprising (i) a M.sup.2+ O component and (ii) a M.sup.2+ Al.sub.2 O.sub.4 spinel component in the same catalyst crystallite and joined through an epitaxial interface, said epitaxial interface being an area in the crystallite where crystalline species of both components (i) and (ii) coexist and form a well defined interface, and wherein M.sup.2+ is Ni.sup.2 + or a mixture of Ni.sup.2 + plus another metal ion or plus other metal ions.
- 15. The composition of claim 14 wherein the heat treating is to a temperature of at least 800.degree. C.
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is a continuation-in-part of application Ser. No. 08/445,699 filed May 22, 1995, now U.S. Pat. No. 5,767,040, which is a continuation-in-part of application Ser. No. 07/993,419 filed Dec. 21, 1992 now abandoned, which applications are specifically incorporated herein in their entirety by reference.
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Continuation in Parts (2)
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Number |
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445699 |
May 1995 |
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Parent |
993419 |
Dec 1992 |
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