IP Library › Granted Patent US 10,611,645
Granted Patent B2
US 10,611,645 · App. 15/658,825 · Granted Apr 7, 2020

Zeolite having a one-dimensional channel system, 10-membered rings and 12-membered rings

Inventors: John P. S. Mowat (Arlington Heights, IL); Wharton Sinkler (Des Plaines, IL); Christopher P. Nicholas (Evanston, IL); Mark A. Miller (Niles, IL); Melissa M. Galey (Chicago, IL)
C01B39/48B01J20/10B01J20/18B01J29/70C01B39/00C01B39/026C07C1/20C07C2/84B01J29/86C01P2002/30C01P2002/72C01P2002/77C01P2004/03C01P2004/04C07C2529/70C07C2529/86Y02P20/52Y02P30/42
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Quick Facts
Patent No.
US 10,611,645
App. No.
15/658,825
Granted
Apr 7, 2020
Kind
B2
Abstract

A new crystalline aluminosilicate zeolite comprising a novel framework has been synthesized that has been designated UZM-55. This zeolite is represented by a three-dimensional framework of at least SiO 2 tetrahedral units and an empirical composition in the as-synthesized and anhydrous basis expressed by an empirical formula of: M m n+ R r Al x E y SiO z where M represents a metal or metals from zinc or Group 1 (IUPAC 1), Group 2 (IUPAC 2), Group 3 (IUPAC 3) or the lanthanide series of the periodic table, R is a structure directing agent or agents such as 1,6-bis(N-methylpiperidinium)hexane, and E is an element selected from the group consisting of gallium, iron, boron and mixtures thereof. Catalysts made from UZM-55 have utility in various hydrocarbon conversion reactions including methanol to hydrocarbons (MTH).

Claims (1045)

1. A microporous crystalline zeolite, UZM-55, having a channel system comprising 10-membered rings of tetrahedrally coordinated atoms and 12-membered rings of tetrahedrally coordinated atoms in a single channel, wherein the channel system is one-dimensional, and represented by an empirical formula:

M m n+ R r Al x E y SiO z

where M represents hydrogen or a metal or metals selected from the group consisting of zinc, Group 1 (IUPAC 1) metals, Group 2 (IUPAC 2) metals, Group 3 (IUPAC 3) metals or lanthanide series metals of the periodic table, “m” is the mole ratio of M to Si and varies from 0 to about 1.0, “n” is the weighted average valence of M and has a value of about 1 to about 3, R is a structure directing agent or agents, “r” is the mole ratio of N from the organic structure directing agent or agents to Si and has a value of about 0 to about 1.0, “x” is the mole ratio of Al to Si and has a value of from 0 to about 0.026, E is an element selected from the group consisting of gallium, iron, boron and mixtures thereof, “y” is the mole ratio of E to Si and has a value from 0 to about 0.026, and “z” is the mole ratio of O to (Al+E) and has a value determined by the equation:

z =(4+ m+ 3● x+ 3● y )/2

and is characterized in that it has the x-ray diffraction pattern having at least the d-spacings and intensities set forth in Table 1:

TABLE 1

2θ

d (Å)

I/I 0 %

7.16

12.34

VW-W

7.44

11.87

VW-W

8.58

10.30

VW

21.01*

4.225

VS

22.07

4.024

VW

22.75

3.906

MW-M

24.19

3.676

VW

26.41

3.372

VW-W

32.73

2.734

VW

36.37

2.468

VW

44.01

2.056

VW.

2. The zeolite of claim 1 wherein the tetrahedrally coordinated atoms are Si, Al or E atoms and have atomic coordinates within ±0.75 Å as shown in Table 3

TABLE 3

Calcined, optimized

Site

X

Y

Z

T1

0.913(3)

0.270(4)

0.745(4)

T2

0.001(3)

0.121(4)

0.633(4)

T3

0.995(3)

0.512(4)

0.373(4)

T4

0.911(3)

0.129(4)

0.983(4)

T5

0.347(3)

0.135(4)

0.940(4)

T6

0.623(3)

0.208(4)

0.828(4)

T7

0.432(3)

0.507(4)

0.581(4)

T8

0.247(3)

0.697(4)

0.335(4)

T9

0.275(3)

0.466(4)

0.500(4)

T10

0.462(3)

0.278(4)

0.765(4)

T11

0.185(3)

0.223(4)

0.870(4)

T12

0.167(3)

0.456(4)

0.701(4)

T13

0.164(3)

0.094(4)

0.694(4)

T14

0.709(3)

0.175(4)

0.498(4)

T15

0.550(3)

0.239(4)

0.417(4)

T16

0.280(3)

0.212(4)

0.514(4)

T17

0.434(3)

0.141(4)

0.606(4)

T18

0.075(3)

0.106(4)

0.057(4)

T19

0.089(3)

0.103(4)

0.296(4)

T20

0.792(3)

0.143(4)

0.164(4)

T21

0.523(3)

0.103(4)

0.262(4)

T22

0.639(3)

0.109(4)

0.081(4)

T23

0.253(3)

0.070(4)

0.364(4)

T24

0.369(3)

0.038(4)

0.192(4)

T25

0.012(3)

0.742(4)

0.610(4)

T26

0.826(3)

0.286(4)

0.313(4)

T27

0.086(3)

0.729(4)

0.254(4)

T28

0.998(3)

0.879(4)

0.367(4)

T29

0.004(3)

0.487(4)

0.626(4)

T30

0.088(3)

0.870(4)

0.016(4)

T31

0.653(3)

0.864(4)

0.059(4)

T32

0.376(3)

0.791(4)

0.171(4)

T33

0.567(3)

0.492(4)

0.418(4)

T34

0.752(3)

0.302(4)

0.664(4)

T35

0.724(3)

0.534(4)

0.499(4)

T36

0.537(3)

0.721(4)

0.234(4)

T37

0.814(3)

0.776(4)

0.129(4)

T38

0.832(3)

0.543(4)

0.299(4)

T39

0.835(3)

0.905(4)

0.305(4)

T40

0.290(3)

0.824(4)

0.501(4)

T41

0.449(3)

0.760(4)

0.582(4)

T42

0.719(3)

0.787(4)

0.485(4)

T43

0.565(3)

0.858(4)

0.393(4)

T44

0.924(3)

0.893(4)

0.942(4)

T45

0.910(3)

0.896(4)

0.704(4)

T46

0.207(3)

0.856(4)

0.835(4)

T47

0.476(3)

0.896(4)

0.737(4)

T48

0.360(3)

0.890(4)

0.918(4)

T49

0.746(3)

0.929(4)

0.635(4)

T50

0.630(3)

0.961(4)

0.807(4)

T51

0.987(3)

0.257(4)

0.389(4)

T52

0.173(3)

0.713(4)

0.686(4).

3. The zeolite of claim 1 wherein the tetrahedrally coordinated atoms are Si, Al or E atoms and have atomic coordinates within ±0.75 Å as shown in Table 4

TABLE 4

Rietveld refinement results

Site

X

Y

Z

T1

0.906(3)

0.259(4)

0.751(4)

T2

0.093(3)

0.740(4)

0.248(4)

T3

0.018(3)

0.119(4)

0.648(4)

T4

0.981(3)

0.880(4)

0.351(4)

T5

0.005(3)

0.504(4)

0.376(4)

T6

0.994(3)

0.495(4)

0.623(4)

T7

0.907(3)

0.123(4)

0.984(4)

T8

0.092(3)

0.876(4)

0.015(4)

T9

0.337(3)

0.141(4)

0.932(4)

T10

0.662(3)

0.858(4)

0.067(4)

T11

0.639(3)

0.204(4)

0.804(4)

T12

0.360(3)

0.795(4)

0.195(4)

T13

0.431(3)

0.510(4)

0.579(4)

T14

0.568(3)

0.489(4)

0.420(4)

T15

0.239(3)

0.709(4)

0.355(4)

T16

0.760(3)

0.290(4)

0.645(4)

T17

0.275(3)

0.479(4)

0.494(4)

T18

0.724(3)

0.520(4)

0.505(4)

T19

0.464(3)

0.267(4)

0.741(4)

T20

0.535(3)

0.732(4)

0.258(4)

T21

0.199(3)

0.233(4)

0.855(4)

T22

0.800(3)

0.767(4)

0.144(4)

T23

0.166(3)

0.467(4)

0.691(4)

T24

0.833(3)

0.532(4)

0.308(4)

T25

0.179(3)

0.096(4)

0.694(4)

T26

0.820(3)

0.903(4)

0.305(4)

T27

0.725(3)

0.149(4)

0.485(4)

T28

0.274(3)

0.851(4)

0.514(4)

T29

0.565(3)

0.218(4)

0.417(4)

T30

0.434(3)

0.781(4)

0.582(4)

T31

0.273(3)

0.204(4)

0.506(4)

T32

0.726(3)

0.795(4)

0.493(4)

T33

0.433(3)

0.136(4)

0.586(4)

T34

0.566(3)

0.863(4)

0.413(4)

T35

0.068(3)

0.138(4)

0.010(4)

T36

0.931(3)

0.861(4)

0.989(4)

T37

0.074(3)

0.093(4)

0.277(4)

T38

0.925(3)

0.906(4)

0.722(4)

T39

0.801(3)

0.139(4)

0.175(4)

T40

0.198(3)

0.860(4)

0.824(4)

T41

0.537(3)

0.098(4)

0.235(4)

T42

0.462(3)

0.902(4)

0.764(4)

T43

0.653(3)

0.113(4)

0.068(4)

T44

0.346(3)

0.886(4)

0.931(4)

T45

0.241(3)

0.072(4)

0.356(4)

T46

0.758(3)

0.927(4)

0.643(4)

T47

0.370(3)

0.057(4)

0.182(4)

T48

0.629(3)

0.942(4)

0.817(4)

T49

0.002(3)

0.761(4)

0.593(4)

T50

0.997(3)

0.238(4)

0.406(4)

T51

0.833(3)

0.267(4)

0.318(4)

T52

0.166(3)

0.732(4)

0.681(4).

4. The microporous crystalline zeolite of claim 1 comprising a framework of tetrahedral atoms bridged by oxygen atoms, the tetrahedral framework being defined by a unit cell of a=17.80 Å, b=12.23 Å, c=12.93 Å, alpha=71.79°, beta=88.16°, gamma=90.25° with fractional atomic coordinates shown in Table 3 or Table 4 wherein each cell axis length may vary within +/−0.75 Å, each cell angle may vary within 1.0° and each t-site position may vary within about +/−0.5 Å wherein Tables 3 and 4 is as follows:

TABLE 3

Calcined, optimized

Site

X

Y

Z

T1

0.913(3)

0.270(4)

0.745(4)

T2

0.001(3)

0.121(4)

0.633(4)

T3

0.995(3)

0.512(4)

0.373(4)

T4

0.911(3)

0.129(4)

0.983(4)

T5

0.347(3)

0.135(4)

0.940(4)

T6

0.623(3)

0.208(4)

0.828(4)

T7

0.432(3)

0.507(4)

0.581(4)

T8

0.247(3)

0.697(4)

0.335(4)

T9

0.275(3)

0.466(4)

0.500(4)

T10

0.462(3)

0.278(4)

0.765(4)

T11

0.185(3)

0.223(4)

0.870(4)

T12

0.167(3)

0.456(4)

0.701(4)

T13

0.164(3)

0.094(4)

0.694(4)

T14

0.709(3)

0.175(4)

0.498(4)

T15

0.550(3)

0.239(4)

0.417(4)

T16

0.280(3)

0.212(4)

0.514(4)

T17

0.434(3)

0.141(4)

0.606(4)

T18

0.075(3)

0.106(4)

0.057(4)

T19

0.089(3)

0.103(4)

0.296(4)

T20

0.792(3)

0.143(4)

0.164(4)

T21

0.523(3)

0.103(4)

0.262(4)

T22

0.639(3)

0.109(4)

0.081(4)

T23

0.253(3)

0.070(4)

0.364(4)

T24

0.369(3)

0.038(4)

0.192(4)

T25

0.012(3)

0.742(4)

0.610(4)

T26

0.826(3)

0.286(4)

0.313(4)

T27

0.086(3)

0.729(4)

0.254(4)

T28

0.998(3)

0.879(4)

0.367(4)

T29

0.004(3)

0.487(4)

0.626(4)

T30

0.088(3)

0.870(4)

0.016(4)

T31

0.653(3)

0.864(4)

0.059(4)

T32

0.376(3)

0.791(4)

0.171(4)

T33

0.567(3)

0.492(4)

0.418(4)

T34

0.752(3)

0.302(4)

0.664(4)

T35

0.724(3)

0.534(4)

0.499(4)

T36

0.537(3)

0.721(4)

0.234(4)

T37

0.814(3)

0.776(4)

0.129(4)

T38

0.832(3)

0.543(4)

0.299(4)

T39

0.835(3)

0.905(4)

0.305(4)

T40

0.290(3)

0.824(4)

0.501(4)

T41

0.449(3)

0.760(4)

0.582(4)

T42

0.719(3)

0.787(4)

0.485(4)

T43

0.565(3)

0.858(4)

0.393(4)

T44

0.924(3)

0.893(4)

0.942(4)

T45

0.910(3)

0.896(4)

0.704(4)

T46

0.207(3)

0.856(4)

0.835(4)

T47

0.476(3)

0.896(4)

0.737(4)

T48

0.360(3)

0.890(4)

0.918(4)

T49

0.746(3)

0.929(4)

0.635(4)

T50

0.630(3)

0.961(4)

0.807(4)

T51

0.987(3)

0.257(4)

0.389(4)

T52

0.173(3)

0.713(4)

0.686(4)

TABLE 4

Rietveld refinement results

Site

X

Y

Z

T1

0.906(3)

0.259(4)

0.751(4)

T2

0.093(3)

0.740(4)

0.248(4)

T3

0.018(3)

0.119(4)

0.648(4)

T4

0.981(3)

0.880(4)

0.351(4)

T5

0.005(3)

0.504(4)

0.376(4)

T6

0.994(3)

0.495(4)

0.623(4)

T7

0.907(3)

0.123(4)

0.984(4)

T8

0.092(3)

0.876(4)

0.015(4)

T9

0.337(3)

0.141(4)

0.932(4)

T10

0.662(3)

0.858(4)

0.067(4)

T11

0.639(3)

0.204(4)

0.804(4)

T12

0.360(3)

0.795(4)

0.195(4)

T13

0.431(3)

0.510(4)

0.579(4)

T14

0.568(3)

0.489(4)

0.420(4)

T15

0.239(3)

0.709(4)

0.355(4)

T16

0.760(3)

0.290(4)

0.645(4)

T17

0.275(3)

0.479(4)

0.494(4)

T18

0.724(3)

0.520(4)

0.505(4)

T19

0.464(3)

0.267(4)

0.741(4)

T20

0.535(3)

0.732(4)

0.258(4)

T21

0.199(3)

0.233(4)

0.855(4)

T22

0.800(3)

0.767(4)

0.144(4)

T23

0.166(3)

0.467(4)

0.691(4)

T24

0.833(3)

0.532(4)

0.308(4)

T25

0.179(3)

0.096(4)

0.694(4)

T26

0.820(3)

0.903(4)

0.305(4)

T27

0.725(3)

0.149(4)

0.485(4)

T28

0.274(3)

0.851(4)

0.514(4)

T29

0.565(3)

0.218(4)

0.417(4)

T30

0.434(3)

0.781(4)

0.582(4)

T31

0.273(3)

0.204(4)

0.506(4)

T32

0.726(3)

0.795(4)

0.493(4)

T33

0.433(3)

0.136(4)

0.586(4)

T34

0.566(3)

0.863(4)

0.413(4)

T35

0.068(3)

0.138(4)

0.010(4)

T36

0.931(3)

0.861(4)

0.989(4)

T37

0.074(3)

0.093(4)

0.277(4)

T38

0.925(3)

0.906(4)

0.722(4)

T39

0.801(3)

0.139(4)

0.175(4)

T40

0.198(3)

0.860(4)

0.824(4)

T41

0.537(3)

0.098(4)

0.235(4)

T42

0.462(3)

0.902(4)

0.764(4)

T43

0.653(3)

0.113(4)

0.068(4)

T44

0.346(3)

0.886(4)

0.931(4)

T45

0.241(3)

0.072(4)

0.356(4)

T46

0.758(3)

0.927(4)

0.643(4)

T47

0.370(3)

0.057(4)

0.182(4)

T48

0.629(3)

0.942(4)

0.817(4)

T49

0.002(3)

0.761(4)

0.593(4)

T50

0.997(3)

0.238(4)

0.406(4)

T51

0.833(3)

0.267(4)

0.318(4)

T52

0.166(3)

0.732(4)

0.681(4).

5. The microporous crystalline zeolite of claim 1 containing planar faults.

6. The microporous crystalline zeolite of claim 5 wherein the planar faults are an offset of about ⅓ of a b axis of said microporous crystalline zeolite.

7. The microporous crystalline zeolite of claim 1 that in a calcined form is characterized in that it has the x-ray diffraction pattern having at least the d-spacings and intensities set forth in Table 2

TABLE 2

2θ

d (Å)

I/I 0 %

7.19

12.28

MW-S

7.57

11.67

W-M

8.59

10.29

W-MW

14.72

6.013

VW

21.04*

4.219

VS

22.15

4.010

VW

23.03

3.859

MW-M

24.34

3.654

VW

26.63

3.345

VW-W

36.47

2.462

VW

44.49

2.035

VW.

8. A method of preparing a microporous crystalline zeolite, UZM-55, having a channel system comprising 10-membered rings of tetrahedrally coordinated atoms and 12-membered rings of tetrahedrally coordinated atoms in a single channel, wherein the channel system is one-dimensional, and represented by an empirical formula:

M m n+ R r Al x E y SiO z

where M represents hydrogen or a metal or metals selected from the group consisting of zinc, Group 1 (IUPAC 1) metals, Group 2 (IUPAC 2) metals, Group 3 (IUPAC 3) metals or lanthanide series metals of the periodic table, “m” is the mole ratio of M to Si and varies from about 0 to about 1.0, “n” is the weighted average valence of M and has a value of about 1 to about 3, R is a structure directing agent or agents, “r” is the mole ratio of N from the organic structure directing agent or agents to Si and has a value of about 0 to about 1.0, “x” is the mole ratio of Al to Si and has a value of from 0 to about 0.026, E is an element selected from the group consisting of gallium, iron, boron and mixtures thereof, “y” is the mole ratio of E to Si and has a value from 0 to about 0.026, and “z” is the mole ratio of O to (Al+E) and has a value determined by the equation:

z =(4+ m+ 3● x+ 3● y )/2

and is characterized in that it has the x-ray diffraction pattern having at least the d-spacings and intensities set forth in Table 1:

TABLE 1

2θ

d(Å)

I/I 0 %

7.16

12.34

VW-W

7.44

11.87

VW-W

8.58

10.30

VW

21.01*

4.225

VS

22.07

4.024

VW

22.75

3.906

MW-M

24.19

3.676

VW

26.41

3.372

VW-W

32.73

2.734

VW

36.37

2.468

VW

44.01

2.056

VW

the process comprising:

preparing a reaction mixture having composition expressed in terms of mole ratios of the oxides of

a M 2 O: b R: c Al 2 O 3 :e E 2 O 3 :SiO 2 :g H 2 O

where M represents a metal or metals from hydrogen, zinc or Group 1 (IUPAC 1), Group 2 (IUPAC 2), Group 3 (IUPAC 3) or the lanthanide series of the periodic table, “a” has a value from 0 to about 0.5,

R is an organic structure directing agent or agents wherein R has a formula [bis-N,N′-diR 1 -(piperidinium)-R 2 ] 2+ 2X − , R 1 is selected from H or an alkyl group having a formula C q H 2q+I , where q is in the range from 1 to 4, X is halide or hydroxide, the total number of C atoms in the formula is in a range of 11 to 24, and R 2 is an alkyl group having the formula C p H 2p , where p is equal to 6 and is connected to the 1 and 1′ N atoms at positions s and t of the alkyl chain where s and t are independently selected from 1 to p,

and where the source of R is a pre-reacted aqueous solution wherein pre-reaction comprises preparing an aqueous mixture comprising water, a substituted hydrocarbon and an amine; reacting the aqueous mixture; obtaining a solution comprising the organoammonium compound; and wherein the mixture and the solution are essentially free of aluminum and silicon, where the pre-reaction temperature is from about 20° C. to about 100° C., and for a time from about 0.5 hours to about 48 hours,

“b” has a value from about 0 to about 0.3,

“c” has a value of from 0.0 to about 0.015,

E is an element selected from the group consisting of gallium, iron, boron and mixtures thereof,

“e” has a value from 0.0 to about 0.015,7 and

“g” has a value from about 20 to about 40;

reacting the reaction mixture at a temperature of about 150° to about 185° C. for a period of time of about 1 day to about 3 weeks under autogenous pressure until crystallization is complete;

isolating a solid product; and

washing the solid product with deionized water and drying the solid product.

9. The method of claim 8 further comprising adding UZM-55 seeds to the reaction mixture.

10. The method of claim 8 wherein a source for M is selected from the group consisting of sodium hydroxide, potassium hydroxide, sodium aluminate, potassium aluminate, sodium silicate, and potassium silicate.

11. The method of claim 8 wherein a source for E is selected from the group consisting of alkali borates, boric acid, precipitated gallium oxyhydroxide, gallium sulfate, ferric sulfate, ferric chloride and mixtures thereof and a source for aluminum is selected from the group consisting of aluminum alkoxides, precipitated aluminas, aluminum metal, aluminum hydroxide, sodium aluminate, potassium aluminate, aluminum salts and alumina sols.

12. The method of claim 8 wherein a source for silica is selected from the group consisting of tetraethylorthosilicate, colloidal silica, fumed silica, precipitated silica and alkali silicates.

13. The method of claim 8 further comprising modifying said microporous crystalline zeolite by one or more modifications selected from the group consisting of calcination, ion-exchange, steaming, acid extraction and ammonium hexafluorosilicate treatment.

14. A hydrocarbon conversion process comprising contacting the hydrocarbon with a microporous crystalline zeolite, UZM-55, having a channel system comprising 10-membered rings of tetrahedrally coordinated atoms and 12-membered rings of tetrahedrally coordinated atoms in a single channel and represented by an empirical formula:

M m n+ R r Al x E y SiO z

where M represents hydrogen or a metal or metals selected from the group consisting of zinc, Group 1 (IUPAC 1) metals, Group 2 (IUPAC 2) metals, Group 3 (IUPAC 3) metals or lanthanide series metals of the periodic table, “m” is the mole ratio of M to Si and varies from 0 to about 1.0, “n” is the weighted average valence of M and has a value of about 1 to about 3, R is a structure directing agent or agents, “r” is the mole ratio of N from the organic structure directing agent or agents to Si and has a value of about 0 to about 1.0, “x” is the mole ratio of Al to Si and has a value of from 0 to about 0.026, E is an element selected from the group consisting of gallium, iron, boron and mixtures thereof, “y” is the mole ratio of E to Si and has a value from 0 to about 0.026, and “z” is the mole ratio of O to (Al+E) and has a value determined by the equation:

z =(4+ m+ 3● x+ 3● y )/2

and is characterized in that it has the x-ray diffraction pattern having at least the d-spacings and intensities set forth in Table 1:

TABLE 1

2θ

d(Å)

I/I 0 %

7.16

12.34

VW-W

7.44

11.87

VW-W

8.58

10.30

VW

21.01*

4.225

VS

22.07

4.024

VW

22.75

3.906

MW-M

24.19

3.676

VW

26.41

3.372

VW-W

32.73

2.734

VW

36.37

2.468

VW

44.01

2.056

VW

wherein said contact is at conversion conditions to provide a converted hydrocarbon product wherein the hydrocarbon conversion process is selected from the group consisting of conversion of methanol to olefins, ethylene to propylene, oligomerization, isomerization of paraffins, paraffin cracking, xylene isomerization, toluene disproportionation, ring opening and cracking to remove benzene co-boilers and alkylation of aromatics with paraffins.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 28, 2017
From: MOWAT, JOHN P.S.; SINKLER, WHARTON; NICHOLAS, CHRISTOPHER P.; MILLER, MARK A.; GALEY, MELISSA M.
To: UOP LLC
Reel/Frame 043418/0988 →
Continuity (2)
Provisional Application 62405055 · Oct 6, 2016
Related Publication 20180099875A1 · Apr 12, 2018
Cited By (1)
US 12,390,800