Silver impregnation method for producing ethylene oxide catalyst with enhanced catalytic ability

Patent metadata

Field	Value
Publication number	US-2018201595-A1
Application number	US-201815873125-A
Country	US
Kind code	A1
Filing date	Jan 17, 2018
Priority date	Jan 17, 2017
Publication date	Jul 19, 2018
Grant date	—

Abstract

A method for producing a catalyst effective in the oxidative conversion of ethylene to ethylene oxide, the method comprising: (i) impregnating a porous refractory carrier with a sub-catalytic level of silver ion in a range of 0.1 wt % to 1 wt % of silver by weight of the carrier and silver, and at least partially reducing said silver ion to elemental silver to produce a low-silver catalyst precursor having isolated silver atoms or silver nanoparticles on surfaces of said refractory carrier; and (ii) further impregnating the low-silver catalyst precursor with a catalytic amount of silver ion of at least 10 wt % total amount of silver and at least one promoting species by weight of the carrier and silver, and subjecting the further impregnated carrier to an elevated temperature of at least 200° C. to completely reduce silver ion to elemental silver in the carrier. The low-silver catalyst precursor produced in step (i) is also described in detail. Methods for using the catalyst produced in step (ii) for the oxidative conversion of ethylene to ethylene oxide are also described.

First claim

What is claimed is:

1 . A method for producing a catalyst effective in the oxidative conversion of ethylene to ethylene oxide, the method comprising:
(i) impregnating a porous refractory carrier with a sub-catalytic level of silver ion in a range of 0.01 wt % to 1 wt % of silver per total weight of the refractory carrier and silver, and at least partially reducing said silver ion to elemental silver to produce a low-silver catalyst precursor having isolated silver atoms or silver nanoparticles on surfaces of said refractory carrier; and (ii) impregnating the low-silver catalyst precursor with a catalytic amount of silver ion of at least 10 wt % total amount of silver per total weight of the refractory carrier and silver, and also impregnating the low-silver catalyst precursor with at least one inorganic promoting species that promotes the oxidative conversion of ethylene to ethylene oxide and that is included in a catalytically promoting amount, and subjecting the refractory carrier having a catalytic level of silver ion to a calcination process in which the refractory carrier having a catalytic level of silver ion is subjected to an elevated temperature of at least 200° C. to completely reduce silver ion to elemental silver in said refractory carrier, to produce said catalyst effective in the oxidative conversion of ethylene to ethylene oxide.

2 . The method of claim 1 , wherein said sub-catalytic level of silver is in a range of 0.01 wt % to less than 1 wt % of silver per total weight of the refractory carrier and silver.

3 . The method of claim 1 , wherein said sub-catalytic level of silver is in a range of 0.01 wt % to 0.5 wt % of silver per total weight of the refractory carrier and silver.

4 . The method of claim 1 , wherein said sub-catalytic level of silver is in a range of 0.01 wt % to 0.3 wt % of silver per total weight of the refractory carrier and silver.

5 . The method of claim 1 , wherein said silver nanoparticles in step (i) have a size less than 10 nm in diameter.

6 . The method of claim 1 , wherein said silver nanoparticles in step (i) have a size of up to 5 nm in diameter.

7 . The method of claim 1 , wherein said silver nanoparticles in step (i) have a size of up to 2 nm in diameter.

8 . The method of claim 1 , wherein the elevated temperature of at least 100° C. in step (i) is an elevated temperature of at least 200° C.

9 . The method of claim 1 , wherein said at least one inorganic promoting species is selected from the group consisting of alkali, alkaline earth, main group, and transition metal elements other than silver.

10 . The method of claim 1 , wherein said at least one inorganic promoting species is selected from the group consisting of cesium (Cs), lithium (Li), tungsten (W), fluorine (F), phosphorus (P), gallium (Ga), rhenium (Re), and sulfur (S).

11 . The method of claim 1 , wherein said at least one inorganic promoting species is selected from the group consisting of Re, Cs, and Li.

12 . The method of claim 1 , wherein said at least one inorganic promoting species comprises Re.

13 . The method of claim 1 , wherein said catalytic amount of silver in step (ii) is a catalytic amount of silver of at least 15 wt %.

14 . The method of claim 1 , wherein the refractory carrier is comprised of an alumina.

15 . The method of claim 1 , wherein said catalyst effective in the oxidative conversion of ethylene to ethylene oxide, as produced in step (ii), exhibits at least one of an improved catalyst activity, selectivity, and stability, compared to a catalyst produced by impregnating the refractory carrier with said catalytic amount of silver ion of at least 10 wt % and said at least one inorganic promoting species in a single impregnation step, without step (i), followed by calcination at said elevated temperature of at least 200° C.

16 . The method of claim 1 , wherein said catalyst effective in the oxidative conversion of ethylene to ethylene oxide, as produced in step (ii), possesses a greater coverage of said at least one inorganic promoting species on said elemental silver, compared to a catalyst produced by impregnating the refractory carrier with said catalytic amount of silver ion of at least 10 wt % and said at least one inorganic promoting species in a single impregnation step, without step (i), followed by calcination at said elevated temperature of at least 200° C.

17 . The method of claim 1 , wherein the refractory carrier is impregnated with said sub-catalytic level of silver in step (i) by contacting the porous refractory carrier with a silver-containing solution containing the sub-catalytic level of silver in the form of a silver salt under conditions where the silver-containing solution becomes infused into the porous refractory carrier.

18 . The method of claim 1 , wherein the low-silver catalyst precursor is impregnated with said catalytic amount of silver in step (ii) by contacting the low-silver catalyst precursor with a silver-containing solution containing the catalytic level of silver in the form of a silver salt under conditions where the silver-containing solution becomes infused into the porous refractory carrier.

19 . A low-silver catalyst precursor comprising a porous refractory carrier and a sub-catalytic level of silver in a range of 0.01 wt % to 1 wt % of silver per total weight of the refractory carrier and silver, wherein said silver comprises isolated silver atoms or silver nanoparticles on surfaces of said refractory carrier.

20 . The catalyst precursor of claim 19 , wherein said sub-catalytic level of silver is in a range of 0.01 wt % to less than 1 wt % of silver per total weight of the refractory carrier and silver.

21 . The catalyst precursor of claim 19 , wherein said sub-catalytic level of silver is in a range of 0.01 wt % to 0.5 wt % of silver per total weight of the refractory carrier and silver.

22 . The catalyst precursor of claim 19 , wherein said sub-catalytic level of silver is in a range of 0.01 wt % to 0.3 wt % of silver per total weight of the refractory carrier and silver.

23 . The catalyst precursor of claim 19 , wherein said silver nanoparticles have a size less than 10 nm in diameter.

24 . The catalyst precursor of claim 19 , wherein said nanoparticles have a size of up to 5 nm in diameter.

25 . The catalyst precursor of claim 19 , wherein said silver nanoparticles have a size of up to 2 nm in diameter.

26 . The catalyst precursor of claim 19 , wherein said porous refractory carrier is comprised of an alumina.

Assignees

• Scient Design Co

Inventors

• Pak Serguei

Classifications

• B01J23/66

  Silver or gold · CPC title

• C07D301/10 Primary

  with catalysts containing silver or gold · CPC title

• C01G5/00

  Compounds of silver · CPC title

• C01P2004/64

  Nanometer sized, i.e. from 1-100 nanometer · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title