Modified zeolite catalyst and methods for producing and using same

Patent metadata

Field	Value
Publication number	US-2016107153-A1
Application number	US-201414888043-A
Country	US
Kind code	A1
Filing date	May 8, 2014
Priority date	May 10, 2013
Publication date	Apr 21, 2016
Grant date	—

Abstract

The invention pertains to a zeolite catalyst, methods of making same, and its use in the catalytic cracking of naphtha for the production of lower molecular weight olefins and alkanes, while minimizing production less desirable products. A zeolite is modified by base leaching and by the addition of a metal cation, thereby lowering the Si/Al 2 ratio and improving the stability of the formed catalyst.

First claim

1 . A method of modifying a zeolite catalyst comprising:
providing a zeolite catalyst; contacting the provided zeolite catalyst with a first composition comprising NaOH and Na 2 CO 3 , thereby producing a leached zeolite catalyst; contacting the leached zeolite catalyst with a second composition comprising a realuminating agent, thereby producing a realuminated zeolite catalyst; modifying the provided zeolite catalyst, the leached zeolite catalyst, or the realuminated zeolite with one or more metal atoms or ions comprising Mg, Ba, Sr, Cr, Fe, Co, Ni, Cu, Zn, Ga, Ce, Ag, Pd, Bi, Ti, V, Zr, Mo, W, Li, or La, or a mixture thereof; wherein the method produces a modified zeolite catalyst.

2 . The method of claim 1 , wherein the realuminating agent comprises NaAlO 2 , KAlO 2 , or a combination thereof.

3 . The method of claim 1 , wherein the provided zeolite catalyst comprises HZSM-5.

4 . The method of claim 1 , wherein the provided zeolite catalyst has a Si/Al 2 ratio of 27.

5 . The method of claim 1 , wherein the first composition comprises 0.05 M NaOH and 0.8 M Na 2 CO 3 .

6 . The method of claim 1 , wherein the second composition comprises from 0.5 mmol to 4.0 mmol of Al per gram of leached zeolite catalyst.

7 . The method of claim 1 , wherein the metal atom or ion comprises Ti.

8 . The method of claim 1 , wherein modifying the provided zeolite catalyst, the leached zeolite catalyst, or the realuminated zeolite with a metal atom or ion comprises contacting the provided zeolite catalyst, the leached zeolite catalyst, or the realuminated zeolite with third composition comprising TiCl 4 or Ti-isopropoxide.

9 . The method of claim 1 , wherein the metal loading of the modified zeolite catalyst is from 0.5% to 10.0% by weight.

10 . The method of claim 1 , wherein the method further comprises converting the modified zeolite catalyst into the H-form.

11 . A modified zeolite catalyst produced according to the method of claim 1 .

12 . The modified zeolite catalyst of claim 11 , wherein the modified zeolite catalyst produces benzene, toluene, and xylene in combination in an amount of less than 0.8% by weight when the modified zeolite catalyst is contacted with naphtha in a straight run naphtha process, wherein the naphtha comprises 54.7% by weight alkane, 34.2% by weight iso-alkane, 9.6% by weight naphthenes, and 1.5% by weight aromatics.

13 . The modified zeolite catalyst of claim 11 , wherein modified zeolite catalyst remains active after being contacted with the naphtha in the straight run naphtha process for 6 h.

14 . A method of cracking naphtha comprising contacting naphtha with the modified zeolite catalyst of claim 11 .

15 . The method of claim 14 , wherein the method produces ethylene and propylene in combination in a yield of greater than 45%.

16 . The method of claim 14 , wherein the selectivity of the method for the production of ethylene and propylene in combination is in a yield of greater than 58%.

17 . (canceled)

18 . The method of claim 14 , wherein the method produces ethylene and propylene in a ratio less than 0.9.

19 . (canceled)

20 . The method of claim 14 , wherein the method produces benzene, toluene, and xylene in combination in an amount of less than 0.8% by weight when the modified zeolite catalyst is contacted with naphtha in a straight run naphtha process, wherein the naphtha comprises 54.7% by weight alkane, 34.2% by weight iso-alkane, 9.6% by weight naphthenes, and 1.5% by weight aromatics.

21 . The method of claim 14 , wherein the contacting occurs in the presence of steam.

22 . A method of cracking naphtha comprising contacting naphtha with a modified zeolite catalyst produced according to the method of claim 1 .

Assignees

• Saudi Basic Ind Corp

Inventors

• Al-Yassir Nabil
• Al-Hazmi Mohammed
• Siddiqui Mohammed Abdul Bari
• Jin Yaming
• Aitani Abdullah
• Al-Khattaf Sulaiman

Classifications

• B01J29/405

  containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead · CPC title

• B01J37/0203

  the impregnation liquid containing organic compounds · CPC title

• B01J29/44

  Noble metals · CPC title

• B01J37/0201

  Impregnation · CPC title

• B01J29/064

  containing iron group metals, noble metals or copper · CPC title