초록 ▼

In a process for concentrating an at least partially crystalline solid containing at least one zeolite in a mixture comprising at least one auxiliary, for example a template compound, and said solid, the mixture is ultrafiltrated in a step (II) to divide the mixture into a retentate and a permeate,

In a process for concentrating an at least partially crystalline solid containing at least one zeolite in a mixture comprising at least one auxiliary, for example a template compound, and said solid, the mixture is ultrafiltrated in a step (II) to divide the mixture into a retentate and a permeate, the solids content in the retentate being higher than that in the mixture and the solids content in the permeate being lower than that in the mixture. This procedure allows auxiliaries, in particular template compounds, present in the permeate to be recycled into a crystallizing step (I) upstream of step (II).

대표청구항 ▼

1. A process for concentrating an at least partially crystalline solid containing at least one zeolite from a mixture comprising a mother liquor, at least one template compound and said solid, which comprises ultrafiltrating the mixture in a step (II) to divide the mixture into a retentate and a per

1. A process for concentrating an at least partially crystalline solid containing at least one zeolite from a mixture comprising a mother liquor, at least one template compound and said solid, which comprises ultrafiltrating the mixture in a step (II) to divide the mixture into a retentate and a permeate, said permeate consisting essentially of the mother liquor,wherein the solids content in the mixture prior to step (II) is from 1 to 20% by weight, and in the retentate subsequent to step (II) is from 50 to 80% by weiaht, in each case based on the total weight of the mixture or the retentate, respectively, and wherein the solids content in the permeate does not exceed 1% by weiaht, based on the total weight of the permeate. 2. A process as claimed in claim 1, wherein at least one membrane used for the ultrafiltration and contains separating layers having pore diameters ranging from 10 nm to 500 nm.3. A process as claimed in claim 2, wherein the geometry of the at least one membrane is selected from the group consisting of flat, tubular, multichannel-element, capillary and wound geometries.4. A process as claimed in claim 1, wherein the transmembrane pressure ranges from 0.5 to 20 bar.5. An integrated process for producing a solid containing at least one zeolite, which process comprises,(I) at least partially crystallizing a solid containing at least one zeolite from a synthesis mixture to produce a mixture (I) comprising at least said solid and at least one template compound; (II) concentrating the solid present in the mixture (I) by ultrafiltration to produce a retentate and a permeate, said permeate comprising the at least one template compound; (III) agglomerating or granulating or agglomerating and granulating the solid particles in the retentate from (II), wherein the permeate obtained in (II) or the at least one template compound present therein is at least partially recycled into (I). 6. A process as claimed in claim 5, wherein at least one of the steps of agglomerating or granulating or at least two of these steps is/are selected from the group consisting of:(i) spray drying (ii) fluidized-bed drying (iii) spray drying with integrated fluidized bed (iv) batchwise vacuum contact drying (v) belt drying (vi) fluidized-bed spray granulation drying (vii) continuous contact drying (viii) continuous paste mill drying (ix) microgranulation in a spray tower (x) agglomeration by addition of a binder (xi) agglomeration by changing the pH. 7. A process as claimed in claim 6, wherein, in steps (i) to (xi), at least one additive is added prior to, during or after the respective drying/granulating/agglomerating steps.8. A process as claimed in claim 6, wherein, in steps (i) to (xi), at least one additive is added prior to and after the respective drying/granulating/agglomerating steps.9. A process as claimed in claim 6, wherein, in steps (i) to (xi), at least one additive is added prior to and during the respective drying/granulating/agglomerating steps.10. A process as claimed in claim 6, wherein, in steps (i) to (xi), at least one additive is added during and after the respective drying/granulating/agglomerating steps.11. A process as claimed in claim 6, wherein, in steps (i) to (xi), at least one additive is added prior to, during and after the respective drying/granulating/agglomerating steps.12. A process as claimed in claim 1, wherein step (II) is followed by a shaping step (S), the at least one shaping step being selected from the group consisting of briquetting, pelletizing and sintering.13. A process as claimed in claim 5, wherein step (II) or step (III) is followed by a shaping step (S), the at least one shaping step being selected from the group consisting of briquetting, pelletizing and sintering.14. A process as claimed in claim 1, wherein step (II) is followed by a calcining step (C) at temperatures in excess of 400 C.15. A process as claimed in claim 5, wherein at least one of steps (II) and (III) is followed by a calcining step (C) at temperatures in excess of 400 C.16. The process as claimed in claim 1, wherein the mother liquor does not contain more than 5% by weight of particles of more than 2 nm in size.