Method of pretreating a naphtha

Information

  • Patent Grant
  • 4927521
  • Patent Number
    4,927,521
  • Date Filed
    Tuesday, August 30, 1988
    36 years ago
  • Date Issued
    Tuesday, May 22, 1990
    34 years ago
Abstract
An improved process for pretreating a naphtha comprising contacting said naphtha prior to reforming with a zeolite catalyst containing at least one noble metal and at least one alkali metal.
Description
Claims
  • 1. A method of pretreating a raw naphtha feedstream comprising contacting said naphtha feedstream with a noble metal/alkali metal-containing zeolite naphtha reforming catalyst, said catalyst containing from about 0.1-1.0 wt. % of said noble metal and an amount of said alkali metal which exceeds the cationic exchange capacity of said zeolite, at a pressure of about 0 to about 1000 psig, a temperature of about 550.degree. F. to about 850.degree. F., a hydrogen to hydrocarbon molar ratio of about 0.1 to 1 to about 15 to 1 and a weight hourly space velocity of about 0.5 to about 20, thereby increasing the yield of C.sub.4.sup.+ and C.sub.5.sup.+ gasoline and thereafter catalytically reforming said treated naphtha.
  • 2. The method of claim 1 wherein said noble metal is selected from the group consisting of Pt, Pd, Ir, Rh and Ru or mixtures thereof.
  • 3. The method of claim 1 wherein said noble metal comprises Pt.
  • 4. The method of claim 1 wherein said noble metal comprises Pd.
  • 5. The method of claim 1 wherein said alkali metal is selected from the group consisting of lithium, sodium, potassium, rubidium, and cesium or mixtures thereof.
  • 6. The method of claim 1 wherein said alkali metal comprises lithium.
  • 7. The method of claim 1 wherein said alkali metal comprises cesium.
  • 8. The method of claim 1 wherein said zeolite is selected from the group consisting of ZSM-5, ZSM-11, ZSM-12, ZSM-22, ZSM-23, ZSM-35, ZSM-48, Zeolite beta, and mixtures thereof.
  • 9. The method of claim 8 wherein said zeolite is ZSM-23.
  • 10. The method of claim 8 wherein said zeolite is ZSM-22.
  • 11. The method of claim 8 wherein said zeolite is ZSM-5.
  • 12. The method of claim 8 wherein said zeolite is Zeolite beta.
  • 13. The method of claim 1 wherein said pressure ranges from about 100 to about 800 psig, said temperature ranges from about 550.degree. to 750.degree. F., said hydrogen to hydrocarbon molar ratio ranges from about 3 to 1 to about 7 to 1 and said weight hourly space velocity ranges from about 1 to about 3.
  • 14. The method of claim 1 wherein said catalyst contains an inorganic oxide binder.
  • 15. The method of claim 14 wherein said inorganic oxide binder is selected from the group consisting of alumina, silica and silica-alumina.
  • 16. The method of claim 14 wherein said inorganic oxide binder is alumina.
  • 17. The mixture of claim 1 wherein said naphtha is a C.sub.4.sup.+ naphtha.
  • 18. The method of claim 1 wherein said naphtha is a C.sub.5.sup.+ naphtha.
  • 19. A method for pretreating a C.sub.4.sup.+ or C.sub.5.sup.+ naphtha or mixtures thereof which comprises contacting said naphtha with a Pt-alkali metal containing zeolite naphtha reforming catalyst, said reforming catalyst containing an amount of alkali metal exceeding the cationic exchange capacity of the zeolite at a pressure ranging from about 100 to about 800 psig, a temperature ranging from about 550.degree. to 750.degree. F., a hydrogen to hydrocarbon molar ratio from about 3 to 1 to about 7 to 1 and a weight hourly space ratio ranging from about 1 to 3, and thereby producing increased yields of C.sub.4.sup.+ and C.sub.5.sup. gasolines from subsequent catalytic reforming of said treated naphtha.
  • 20. The method of claim 19 wherein said pretreated naphtha is subsequently reformed in the presence of said pretreatment catalyst.
  • 21. The method of claim 18 wherein said zeolite catalyst is selected from the group consisting of ZSM-5, ZSM-12, ZSM-22, ZSM-23, ZSM-35, ZSM-48, zeolite, and mixtures thereof or their hydrogen form.
  • 22. The method of claim 19 wherein said catalyst is a Zeolite beta catalyst.
  • 23. The method of claim 21 whrein said catalyst is a ZSM-22 catalyst or hydrogen form thereof.
  • 24. The method of claim 21 wherein said catalyst is a ZSM-23 catalyst.
  • 25. The method of claim 22 wherein said catalyst contains as the alkali metal Li or K.
  • 26. The method of claim 23 wherein said catalyst contains as the alkali metal Li or K.
  • 27. The method of claim 24 wherein said catalyst contains as the alkali metal Li or K.
BACKGROUND OF THE INVENTION

This application is related to, Ser. No. 238,677, filed concurrently, entitled CATALYTIC REFORMING WITH IMPROVED ZEOLITE CATALYSTS. This invention relates to an improved method of pretreating a naphtha prior to catalytically reforming same. Catalytic reforming is well known and refers to the treatment of naphtha fractions to improve the octane rating by the production of aromatics. A number of other reactions also occur during reforming, however, hydrocracking reactions are to be particularly minimized because they decrease the yield of gasoline boiling products. However, both C.sub.4.sup.+ and C.sub.5.sup.+ gasolines are maximized by the process of the present invention. There is a high demand for high octane gasoline for use as motor fuels and the like. Accordingly, much research is dedicated to the development of improved reforming catalyst and catalytic reforming processes to produce higher yields of C.sub.4.sup.+ and C.sub.5.sup.+ gasolines. Zeolite Beta has been found to be suited for use in a catalyst for hydrocracking naphtha under mild conditions, (U.S. Pat. No. 3,923,641). However, it is desirous to further treat such catalysts to improve their activity and their stability in acid catalyzed reactions by steaming. The catalyst used in hydrocracking/reforming processes generally contain platinum and high acidity zeolites but have poor C.sub.4.sup.+ and C.sub.5.sup.+ selectivity (U.S. Pat. No. 4,276,151). An example of platinum-containing reforming catalysts is described in U.S. Pat. No. 4,456,527 which relates to a reforming process having "superior" selectivity for dehydrocyclization. It has now been found that higher C.sub.4.sup.+ and C.sub.5.sup.+ gasoline yields can be obtained by pretreating the raw naphtha with a suitable zeolite catalyst prior to reforming. It is therefore, an object of this method to provide an improved process wherein pretreatment of a naphtha using zeolitic catalysts provides significantly higher C.sub.4.sup.+ and C.sub.5.sup.+ gasoline yields than conventional hydrotreating and reforming catalysts. This invention is directed to a process of pretreating a naphtha with a zeolite catalyst containing at least one noble metal and one alkali metal useful for catalytic reforming. Zeolites useful include high silica/alumina zeolite beta, ZSM-23, and other similar ZSM-5 type zeolites. The noble metal loading should be in range of 0.1-1 wt. %, and the alkali metal loading should exceed the cationic exchange capacity of the zeolite component if the improved process results are to be attained. The naphtha may be then more advantageously processed as a reformate. Higher C.sub.4.sup.+ and C.sub.5.sup.+ gasoline yields are obtained. The catalysts described herein are different from U.S. Pat. Nos. 3,783,123 and 4,478,706 which use alkali metal containing zeolite catalysts wherein the zeolites must be specially treated and have exchangeable cations/A10.sub.2.sup.- .ltoreq.1. Furthermore, unlike alkaline earth metal zeolite catalysts which are sensitive to sulfur (U.S. Pat. No. 4,456,527), the present catalysts are stable toward sulfur containing feeds. Further the catalysts in accordance with the invention are sulfur resistant and eliminate the need for careful environmental (Chloride, H.sub.2 O) control. The invention therefore, is also more particularly directed to pretreating naphthas with zeolite catalysts containing a noble metal and having acidity and thereafter catalytically reforming with the same or a different catalyst. Pretreatment results in a reformate feed that produces higher yields of C.sub.4.sup.+ and C.sub.5.sup.+ gasolines.

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