SELF-BONDED ZEOLITE PELLET

Abstract: High porosity, large pore, multicrystalline zeolite ag­ gregates are produced by forming an extrudeable wet mix of suitable composition for the zeolite to be produced, form­ ing said mix into shaped bodies, and drying said pellets by infrared radiation. After drying the pellets or bodies are fired to develop a ceramic bond, and then autoclaved under autogenous pressure to produce the desired zeolite crys­ tals.

Description: This invention relates to a self-bonded molecular sieve product with controlled porosity and a process of manufacturing the same. Self-bonded mordenite bodies can be made as described in U.S. Patent 3,445,184. The resulting products are pure (ire. binderless), strong and porous. This invention results in an improved product with increased pore volume and pore size. It is found that the type of drying has a significant effect on the porosities of self-bonded zeolitic products. Conventional methods of drying such as convective drying either on a belt as a fluidized bed or a combination of air drying at room temperature and convective drying results in products of low porosities. However, when infrared drying is employed the porosities are maximized. Porosity, in the contex of this disclosure, refers to macro pores between the crystals or aggregates of crystals (inter-crystalline) and not to the pores within the zeolitic crystal structures (intra crystalline30 Median pore diameter of these macropores range from about 005 microns to greater than 2.0 microns whereas pores within a zeolitic structure are smaller than 10 Angstrons (0.001 microns). The increase in the size and volume of these macropores increases the rates of diffusion of adsorbates and desorbates in the case of adsorption processes; and increases the rates of diffusion of reactants and products in the case of catalytic reactions or cations in the ion exchange process in which zeolitic products are used. According to Whittmore's patent, extrudates of suitable composition containing Na203 and SiO2 are formed, dried using a conventional technique and heat treated to set the bond resulting in a product strong enough to survive autoclaving under high pressures and temperatures. According to the present invention the drying step in the forming process described above is carried out using driers employing infrared heat. The increase in macroporosity is first evident in the fired ware. The number of pores greater than 0.1 microns is increased so that the median pore diameter is 0.4 microns or greater. Total pore volumes are increased to 0.24 to 0.32 cc/gm. Contrastingly, in Whittmorels fired ware, median pore diameters are typically 0.15 to 0.3 microns with pore volumes of 0.18 to 0.3 cc/gm. In this invention, macropores of the final product are also increased. The number of pores greater than 1.5 microns is increased so that the median pore diameter is 2.0 microns or greater. Pore volumes are increased to 0.3 to 0.4 cc/cm. Whittmore's final products have median pore diameters of 0.8 to 1.9 microns with total pore volume of 018 to 0.3 cc/gm. While this invention is particularly directed to self-bonded mordenite pellets it is applicable to the production of large pore, high pore volume self-bonded synthetic alumino-silicate zeolites of other varieties, such as synthetic faujasites, or zeolites X and y. Invention - Example I Four hundred pounds of mineral mixtures were mixed to form an extrudeable composition as taught in U.S. Patent 3,445,184 and formed into 1/16 diameter pellets. The pellets in a bed no more than about 3 pellets deep, were conveyed under infrared heaters where air tempera- ture in the pellet bed was maintained at 400-5000F. Loss on ignition (LOI) of the dried product was 18-20%, for an 85 second exposure of the pellet bed. It was then calcined at 5000C. in order to set the ceramic bond. Porosity of the fired ware was determined and is shown in Figure 1. The pore volume was 0.315 cc/gm with a median pore diameter of 0.88 microns. This batch of fired ware was autoclaved to form zeolitic structure with a solution of sodium silicate at 380-3900F. for 1,5 5 hours. After cooling, the batch was washed for ten hours to remove sodium silicate solution and dried at 3250F. The final zeolitic product had a pore volume of 0.404 cc/gm with a median pore diameter of 3.0 microns. Comparative Example A In the preparation of the second batch drying was carried out following Whittmore's patent on a convective belt dryer which was maintained at room temperature Fired ware had a pore volume of 0.244 cc/gm with a median pore of only 0.25 microns. The final zeolitic product had a pore volume of 0.279 cc/gm with a median pore diameter of only 1.3 microns. Comparative Example B In the preparation of the third batch drying step in the process outlined in Example 1 was carried out using a room temperature fluid bed drier. Fired ware had a pore volume of 0.335 cc/gm with a pore diameter of 1.1 microns. The final zeolitic product had a pore volume of 0.272 cc/gm with a median pore diameter of 2.1 microns. Comparative Example C In the preparation of the fourth batch the drying step in the process outlined in Example 1 was carried out by a combination of static air drying and forced air drying on a belt, both at room temperature. Thus, a batch was room air dried on trays for 24 hours then forced air dried on a belt to an LOI of 18-20%. LOI (loss on ignition) in this case means the loss in weight when the pellets are heated to 1200C. (air temperature) for twenty minutes. Porosities of fired ware and the final zeolitic products are shown in Figures - and 8. Fired ware had a pore volume of 0.214 cc/gm with a median pore diameter of 0.78 microns. The final zeolitic product had a pore volume of 0.296 cc/gm and a median pore diameter of 1.8 microns. Comparative Example D In the preparation of the fifth batch, the drying step in the process outlined in Example I was carried out on a convection belt drier using heated air. The fired ware had a pore volume of 0.269 cc/gm and a mean pore diameter of 0.24 microns. The final zeolitic product had a pore volume of 0.266 cc/gm and a mean pore diameter of 1.45 microns. A suitable mix for the preparation of mordenite is a mixture of 19.15% Georgia kaolin, 26.57% diatomaceous earth, 54.28% (28.7% Six2, 8.9% Na2O) aqueous sodium silicate, with added water to give a mix of extrudeable consistency, having a mole composition ratio of soda to alumina to silica of 1 to 1 to 10. The mix, after being formed into pellets and dried by infrared radiation, is fired to around 500 C. to form hard strong but not completely vitrified bodies suitable for autoclaving. With the above described mix a suitable composition for the sodium silicate in the autoclave under autogenous pressure at 380 to 3900C. is the mole ration, soda to silica to water of 0.3 to 1 to 8.7, giving a solution of 10 mole % silica.

Claims: CLAIMS 1. A self-bonded zeolite pellet having a median intercrystalline pore diameter of 2 microns of greater and a total inter-crystalline pore volume of greater than 0.3 cubic centimeters per gram. 2. A pellet according to claim 1, consisting essentially of crystalline synthetic mordenite. 3. A pellet according to claim 1, consisting essentially of crystalline synthetic faujasite. 4. A method of making a self-bonded crystalline zeolite agglomerate comprising forming an extrudeable mixture which when autoclaved in sodium silicate solution will produce zeolite crystals, forming said mix into shaped bodies, drying said bodies in air by radiant heating, firing said bodies to produce strongly bonded stable pellets, but below complete vitrification of the mix, and autoclaving said pellets under autogenous pressure whereby the desired zeolite crystals are formed.

Inventors: CRABTREE, ROBERT GLEN, GERDES, WILLIAM HERMAN
Applicants: PQ CORPORATION
Application year: 1984
Main classification: C01B33
IPC codes: C01B39