Process for producing VET-type zeolite
View Patent ↗A process for producing a VET-type zeolite is provided in which the use of a structure-directing agent is minimized and the environmental burden can be minimized. This process for producing a VET-type zeolite comprises (1) mixing a zinc source, an element M 1 source, an alkali source, and water so as to result in a reaction mixture having a specific composition in terms of molar ratio, (2) using, as seed crystals, a VET-type zeolite which has an M 1 O 2 /ZnO ratio of 5-30 and adding the zeolite to the reaction mixture in an amount of 0.1-30 wt % relative to the M 1 O 2 contained in the reaction mixture, and (3) heating the reaction mixture to which the seed crystals have been added, at 80-200° C. in a hermetically closed state. M 1 represents silicon or a mixture of silicon and germanium.
1. A production method for a VET-type zeolite, which comprises
(1) mixing a zinc source, an element M 1 source, an alkali source, and water so as to be a reaction mixture having a composition represented by a molar ratio given below;
M 1 O 2 /ZnO=5-300
(Li 2 O+Na 2 O)/M 1 O 2 =0.1-0.6
Li 2 O/(Li 2 O+Na 2 O)=0.01-0.4
H 2 O/M 1 O 2 =5-50
where M 1 denotes silicon or a mixture of silicon and germanium;
(2) using a VET-type zeolite having an M 1 O 2 /ZnO ratio of 5-30 as a seed crystal, and adding the VET-type zeolite to the reaction mixture at a proportion of 0.1-30% by weight with respect to M 1 O 2 in the reaction mixture; and
(3) airtightly heating the reaction mixture to which the seed crystal has been added at 80-200° C.
2. The production method according to claim 1 , wherein the step (1) comprises mixing the zinc source, the element M 1 source, the alkali source, water, and an element M 2 source so that the reaction mixture has a composition represented by a molar ratio given below:
M 1 O 2 /ZnO=5-300
M 1 O 2 /M 2 O 3 =50-1000
(Li 2 O+Na 2 O)/M 1 O 2 =0.1-0.6
Li 2 O/(Li 2 O+Na 2 O)=0.01-0.4
H 2 O/M 1 O 2 =5-50
where M 2 denotes aluminum, iron, gallium, or a mixture of two or more of these.
3. The production method according to claim 2 , wherein after the reaction mixture not containing the seed crystal is airtightly heated at a temperature of 80-200° C., the seed crystal is added to the reaction mixture, and the reaction mixture is further airtightly heated at a temperature of 80-200° C.
4. The production method according to claim 2 , wherein the reaction mixture is agitated in the airtightly heating process.
5. The production method according to claim 1 , wherein after the reaction mixture not containing the seed crystal is airtightly heated at a temperature of 80-200° C., the seed crystal is added to the reaction mixture, and the reaction mixture is further airtightly heated at a temperature of 80-200° C.
6. The production method according to claim 5 , wherein the reaction mixture is agitated in the airtightly heating process.
7. The production method according to claim 1 , wherein the reaction mixture is agitated in the airtightly heating process.