Catalyst – solid sorbent – or support therefor: product or process – Catalyst or precursor therefor – Phosphorus or compound containing same
Reexamination Certificate
2002-05-22
2003-12-23
Bell, Mark L. (Department: 1755)
Catalyst, solid sorbent, or support therefor: product or process
Catalyst or precursor therefor
Phosphorus or compound containing same
C502S212000, C502S230000, C502S415000, C502S439000, C423S617000, C423S625000, C423S628000, C423S115000, C423S304000, C423S323000, C423S265000, C423S275000, C208S057000, C208S058000, C208S060000, C208S066000, C208S070000, C208S134000, C208S135000, C208S137000, C208S138000, C208S139000
Reexamination Certificate
active
06667270
ABSTRACT:
FIELD OF THE INVENTION
This invention relates to bismuth- and phosphorus-containing catalyst supports, naphtha reforming catalysts made from such supports, methods of making both support and catalyst, and to a naphtha reforming process using such catalysts.
BACKGROUND OF THE INVENTION
Catalytic naphtha reforming is an important oil refining process that converts low-octane paraffins- and naphthenes-rich naphtha to high-octane, aromatics-rich C
5
+liquid reformate and hydrogen (H
2
). Petroleum refiners are always searching for improved reforming catalysts that afford high selectivity (i.e., high C
5
+liquid and H
2
yields), high activity, low coking rates and high selectivity and/or activity stability. More selective catalysts are desired to maximize the production of valuable C
5
+liquid and H
2
while minimizing the yield of less desirable C
1
-C
4
gaseous products. Catalysts with acceptable selectivity but higher activity are also desired because they allow operation at lower reactor inlet temperatures while maintaining the same conversion (octane) level or allow operation at the same temperature but at higher conversion (octane) level. In the former case, the higher activity of the catalysts also allows for significant extension of the cycle length and reduced frequency of regeneration. Catalysts that afford lower coke make rates and higher selectivity and/or activity stability are also very highly desired because they allow for significant shortening of the coke bum off and unit turnaround time or for a longer operation before regeneration.
Many researchers have devoted their efforts to the discovery and development of improved reforming catalysts. The original commercial catalysts employed a platinum-group metal, preferably platinum itself, deposited on a halogen-acidified &ggr;-alumina support; see, for example, Haensel's U.S. Pat. Nos. 2,479,109-110, granted in 1949 and assigned to Universal Oil Products Company. About 1968, the use of rhenium together with platinum was introduced. Kluksdhal's U.S. Pat. No. 3,415,737 teaches Pt/Re catalysts wherein the atomic ratio of rhenium to platinum is between 0.2 and 2.0 and his U.S. Pat. No. 3,558,477 teaches the importance of holding the atomic ratio of rhenium to platinum to less than 1.0. Buss's U.S. Pat. No. 3,578,583 teaches the inclusion of a minor amount, up to 0.1 percent, of iridium in a catalyst having up to 0.3 percent each of rhenium and platinum. Gallagher et al.'s U.S. Pat. No. 4,356,081 teaches a bimetallic reforming catalyst wherein the atom ratio of rhenium to platinum is between 2 and 5.
Phosphorus has been known to increase aromatics yield when included in reforming catalysts since at least 1959 when Haensel taught the same in U.S. Pat. No. 2,890,167. In U.S. Pat. No. 3,706,815, Alley taught that chelating ions of a Group VIII noble metal with polyphosphoric acid in a catalyst enhanced isomerization activity. And Antos et al.'s U.S. Pat. Nos. 4,367,137, 4,416,804, 4,426,279, and 4,463,104 taught that the addition of phosphorus to a noble-metal reforming catalyst results in improved C
5
+yields.
In 1974-5, Wilhelm's U.S. Pat. Nos. 3,798,155, 3,888,763, 3,859,201 and 3,900,387 taught the inclusion of bismuth in a platinum-group reforming catalyst to improve selectivity, activity and stability characteristics. Antos' U.S. Pat. No. 4,036,743 taught a hydrocarbon conversion catalyst comprising platinum, bismuth, nickel and halogen components. More recently, Wu et al.'s U.S. Pat. Nos. 6,083,867 and 6,172,273 B1 teach a reforming catalyst of mixed composition or stage-loaded comprising a first catalyst comprising platinum and rhenium on a porous carrier material and a second catalyst comprising a bismuth and silica component.
Until now, however, no one has taught the benefits of including both bismuth and phosphorus in a noble-metal naphtha reforming catalyst.
SUMMARY OF THE INVENTION
This invention provides for a catalyst support comprising &ggr;-alumina and small amounts of bismuth and phosphorus incorporated homogeneously throughout. The invention further provides for catalyst compositions comprising platinum, chlorine, and optionally rhenium, deposited on such supports. The invention also provides for a method of making such catalyst support and catalyst compositions and for a process for reforming naphtha to improve its octane using such catalyst. When used to catalyze reforming of naphtha, the Bi- and P-containing catalyst compositions of this invention unexpectedly exhibited significantly lower coking rates and C
5
+ yields and activity decline rates; i.e., higher stability, relative to catalysts containing only either Bi or P previously known.
REFERENCES:
patent: 2479109 (1949-08-01), Haensel
patent: 2479110 (1949-08-01), Haensel
patent: 2890167 (1959-06-01), Haensel
patent: 3415737 (1968-12-01), Kluksdahl
patent: 3558477 (1971-01-01), Kluksdahl
patent: 3578583 (1971-05-01), Buss
patent: 3706815 (1972-12-01), Alley, Jr.
patent: 3798155 (1974-03-01), Wilhelm
patent: 3859201 (1975-01-01), Wilhelm
patent: 3888763 (1975-06-01), Wilhelm
patent: 3900387 (1975-08-01), Wilhelm
patent: 4036743 (1977-07-01), Antos
patent: 4356081 (1982-10-01), Gallagher et al.
patent: 4367137 (1983-01-01), Antos et al.
patent: 4416804 (1983-11-01), Antos et al.
patent: 4426279 (1984-01-01), Antos et al.
patent: 4463104 (1984-07-01), Antos et al.
patent: 4522935 (1985-06-01), Robinson et al.
patent: 5905053 (1999-05-01), Rizkalla et al.
patent: 6083867 (2000-07-01), Wu et al.
patent: 6172273 (2001-01-01), Wu et al.
patent: 6183719 (2001-02-01), Muller et al.
patent: 6383967 (2002-05-01), Holmgren et al.
Bell Mark L.
Hailey Patricia L.
Shell Oil Company
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